JPH04371229A - Catalyst composition - Google Patents
Catalyst compositionInfo
- Publication number
- JPH04371229A JPH04371229A JP3144471A JP14447191A JPH04371229A JP H04371229 A JPH04371229 A JP H04371229A JP 3144471 A JP3144471 A JP 3144471A JP 14447191 A JP14447191 A JP 14447191A JP H04371229 A JPH04371229 A JP H04371229A
- Authority
- JP
- Japan
- Prior art keywords
- oxide
- catalyst
- rare earth
- catalyst composition
- perovskite
- 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
- 239000003054 catalyst Substances 0.000 title claims abstract description 29
- 239000000203 mixture Substances 0.000 title claims description 14
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 8
- RVTZCBVAJQQJTK-UHFFFAOYSA-N oxygen(2-);zirconium(4+) Chemical compound [O-2].[O-2].[Zr+4] RVTZCBVAJQQJTK-UHFFFAOYSA-N 0.000 claims abstract description 7
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract description 7
- 229910001928 zirconium oxide Inorganic materials 0.000 claims abstract description 7
- 229910000428 cobalt oxide Inorganic materials 0.000 claims abstract description 6
- IVMYJDGYRUAWML-UHFFFAOYSA-N cobalt(ii) oxide Chemical compound [Co]=O IVMYJDGYRUAWML-UHFFFAOYSA-N 0.000 claims abstract description 6
- TWNQGVIAIRXVLR-UHFFFAOYSA-N oxo(oxoalumanyloxy)alumane Chemical compound O=[Al]O[Al]=O TWNQGVIAIRXVLR-UHFFFAOYSA-N 0.000 claims abstract description 6
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 claims abstract description 4
- 239000011575 calcium Substances 0.000 claims abstract description 4
- 229910052788 barium Inorganic materials 0.000 claims abstract description 3
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 claims abstract description 3
- 229910052791 calcium Inorganic materials 0.000 claims abstract description 3
- 239000002131 composite material Substances 0.000 claims description 12
- 229910001404 rare earth metal oxide Inorganic materials 0.000 claims description 4
- 230000003197 catalytic effect Effects 0.000 abstract description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 18
- 229910052763 palladium Inorganic materials 0.000 description 9
- QVQLCTNNEUAWMS-UHFFFAOYSA-N barium oxide Chemical compound [Ba]=O QVQLCTNNEUAWMS-UHFFFAOYSA-N 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 5
- 230000000052 comparative effect Effects 0.000 description 4
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 3
- IWOUKMZUPDVPGQ-UHFFFAOYSA-N barium nitrate Chemical compound [Ba+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O IWOUKMZUPDVPGQ-UHFFFAOYSA-N 0.000 description 3
- 229910002091 carbon monoxide Inorganic materials 0.000 description 3
- 229910000420 cerium oxide Inorganic materials 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 3
- 239000000843 powder Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000004817 gas chromatography Methods 0.000 description 2
- 239000001307 helium Substances 0.000 description 2
- 229910052734 helium Inorganic materials 0.000 description 2
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910002210 La0.9Ce0.1CoO3 Inorganic materials 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- ODINCKMPIJJUCX-UHFFFAOYSA-N calcium oxide Inorganic materials [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- JSKIRARMQDRGJZ-UHFFFAOYSA-N dimagnesium dioxido-bis[(1-oxido-3-oxo-2,4,6,8,9-pentaoxa-1,3-disila-5,7-dialuminabicyclo[3.3.1]nonan-7-yl)oxy]silane Chemical compound [Mg++].[Mg++].[O-][Si]([O-])(O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2)O[Al]1O[Al]2O[Si](=O)O[Si]([O-])(O1)O2 JSKIRARMQDRGJZ-UHFFFAOYSA-N 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000000691 measurement method Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- GPNDARIEYHPYAY-UHFFFAOYSA-N palladium(ii) nitrate Chemical compound [Pd+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O GPNDARIEYHPYAY-UHFFFAOYSA-N 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000012495 reaction gas Substances 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 239000010948 rhodium Substances 0.000 description 1
- MHOVAHRLVXNVSD-UHFFFAOYSA-N rhodium atom Chemical compound [Rh] MHOVAHRLVXNVSD-UHFFFAOYSA-N 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】本発明は、排気ガス中に含まれる
炭化水素(HC)、一酸化炭素(CO)及び窒素酸化物
(NOX )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気ガス浄化用触媒等に用いられる
触媒組成物に関する。[Industrial Application Field] The present invention converts hydrocarbons (HC), carbon monoxide (CO), and nitrogen oxides (NOX) contained in exhaust gas into water, carbon dioxide gas, and nitrogen through oxidation or reduction reactions. The present invention relates to a catalyst composition for use in exhaust gas purification catalysts and the like.
【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合公報
)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。[Prior Art] Conventional catalyst compositions of this type include those consisting of rare earth element oxides, perovskite-type composite oxides, and palladium (Japanese Unexamined Patent Publication No. 156349/1983), and those containing perovskite-type composite oxides on the surface. There has been a catalyst carrier provided with a layer containing a rare earth oxide having storage properties and supporting palladium or palladium and other noble metals as a catalyst component (Japanese Patent Application Laid-Open No. 162948/1983).
【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。[Problems to be Solved by the Invention] However, when the above-mentioned conventional catalyst composition is used for a long time in a reducing atmosphere at a high temperature of 200°C or higher, noble metals such as palladium may cause grain growth and may cause grain growth in the perovskite-type composite oxide. There was a problem that the durability was poor, such as the catalytic activity gradually decreasing 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 solves the above problems and aims to provide a catalyst composition with 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ジルコニウム
と酸化アルミニウムと酸化コバルトとカルシウムまたは
バリウムのうち1種類以上の酸化物及び貴金属のうちの
1種以上からなる。[Means for Solving the Problems] In order to achieve the above object, the catalyst composition of the present invention comprises a perovskite-type composite oxide containing a rare earth element, a rare earth oxide, zirconium oxide, aluminum oxide, cobalt oxide, and calcium or barium oxide. It consists of one or more kinds of oxides and one or more kinds 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。[Function] With the above structure, the present invention suppresses the grain growth of noble metals and the diffusion into the perovskite composite oxide 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10
0g、酸化セリウム(CeO2 )の粉末80g、酸化
ジルコニウム(ZrO2 )の粉末20g、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と硝酸コバルト〔
Co(NO3 )2 〕4.5g、及び硝酸バリウム〔
Ba(NO3 )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400セル/(インチ)2 のコーディエラ
イト(2MgO・5SiO2 ・2Al2 O2 )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。その後担体を200℃で1
時間乾燥し、650℃で1時間焼成して触媒組成物約2
4重量%、担体約76重量%の排気ガス浄化用触媒体を
得た。触媒組成物中のペロブスカイト型複合酸化物は4
7.8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%、酸化コバルトは0.28重
量%、酸化バリウムは0.56重量%であった。Powder 10 of perovskite type composite oxide containing rare earth element La0.9Ce0.1CoO3
0g, 80g of cerium oxide (CeO2) powder, 20g of zirconium oxide (ZrO2) powder, 50g of alumina sol (acidic acid, solid content 1/10), 0.9g of palladium nitrate [Pd(NO3)2] and cobalt nitrate [
Co(NO3)2] 4.5 g, and barium nitrate [
A slurry was prepared by mixing and stirring 4.2 g of Ba(NO3)2 and 150 g of water. A honeycomb carrier made of cordierite (2MgO.5SiO2.2Al2 O2) having a lattice-like cross section and having a cross section of 400 cells/(inch)2 was immersed in the slurry, pulled up, and then the excess slurry was blown off by an air stream. After that, the carrier was heated to 200℃ for 1
After drying for 1 hour and calcining at 650°C for 1 hour, the catalyst composition
An exhaust gas purifying catalyst body containing 4% by weight and about 76% by weight of the carrier was obtained. The perovskite type composite oxide in the catalyst composition is 4
7.8% by weight, aluminum oxide 2.40% by weight, palladium 0.27% by weight, cobalt oxide 0.28% by weight, and barium oxide 0.56% 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ジルコニ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 supporting a catalyst composition consisting of a perovskite-type composite oxide, cerium oxide, zirconium oxide, aluminum oxide, and palladium (Comparative Example 1) and a catalyst composition consisting of a perovskite-type composite oxide and palladium were prepared. A catalyst body (Comparative Example 2) supporting the following 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。[0010] The three types of catalyst bodies produced above were compared in terms of initial characteristics and durability of catalyst performance.
【0011】試験条件は次の通りであり、試験結果を表
1に示す。The test conditions were as follows, and the test results are shown in Table 1.
【0012】0012
【表1】[Table 1]
【0013】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
性に対しては酸化コバルト及び酸化バリウムの存在が必
須であることが明かである。Catalyst performance test conditions (1) Gas composition (volume basis) A reaction gas consisting of 1% NO, 1% CO, and 98% helium was used. ■Space velocity: 12,500/Hr ■Measurement method The reaction was carried out using a fixed bed flow system, and the conversion rate of NO to N2 was determined by gas chromatography. The reaction temperature is 300°C. From the same table, it is clear that the presence of cobalt oxide and barium oxide is essential for the durability of catalyst performance.
【0014】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。[0014] Next, the changes in catalytic performance over time of the three types of catalyst bodies mentioned above were measured, and the results shown in FIG. 1 were obtained. From the figure, the catalyst body of this example showed excellent durability.
【0015】この時の試験条件は次の通りである。触媒
を900℃の電気炉で空気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3
00℃である。The test conditions at this time were as follows. The catalyst was treated in an electric furnace at 900°C under an air atmosphere, and changes in activity were examined. ■Gas composition (volume basis) NO1% CO1% Helium 98% ■Space velocity
12500/Hr (2) Measuring method The reaction was carried out using a fixed bed flow system, and the conversion rate of NO to N2 was determined by gas chromatography. The reaction temperature is 3
It is 00℃.
【0016】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, similar effects can be obtained by using platinum or rhodium in part or in whole in addition to palladium.
【0017】[0017]
【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ジルコニウムと酸化アルミニウムと
酸化コバルトと、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への拡散を抑制する耐
久性の優れた触媒である。As explained above, the catalyst composition of the present invention comprises a perovskite-type composite oxide containing a rare earth element, a rare earth oxide, zirconium oxide, aluminum oxide, cobalt oxide, and one or more of calcium or barium. It is a highly durable catalyst that suppresses grain growth and diffusion of noble metals into perovskite composite oxides even in high-temperature atmospheres of 500° C. or higher.
【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] A diagram showing the durability of catalyst performance of an example of the present invention and a comparative example.
Claims (1)
合酸化物と希土類酸化物と酸化ジルコニウムと酸化アル
ミニウムと酸化コバルトと、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
上からなる触媒組成物。Claim 1: A perovskite-type composite oxide containing a rare earth element, a rare earth oxide, zirconium oxide, aluminum oxide, cobalt oxide, one or more oxides of calcium or barium, and one or more noble metals. A catalyst composition consisting of:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3144471A JPH04371229A (en) | 1991-06-17 | 1991-06-17 | Catalyst composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3144471A JPH04371229A (en) | 1991-06-17 | 1991-06-17 | Catalyst composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04371229A true JPH04371229A (en) | 1992-12-24 |
Family
ID=15363063
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3144471A Pending JPH04371229A (en) | 1991-06-17 | 1991-06-17 | Catalyst composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04371229A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007072690A1 (en) * | 2005-12-22 | 2007-06-28 | Cataler Corporation | Catalyst for exhaust gas clean-up |
WO2008004390A1 (en) * | 2006-07-05 | 2008-01-10 | Cataler Corporation | Catalyst for purifying exhaust gas and process for producing the same |
JP2020513295A (en) * | 2016-11-14 | 2020-05-14 | リサーチ トライアングル インスティテュート | Perovskite catalyst and its use |
-
1991
- 1991-06-17 JP JP3144471A patent/JPH04371229A/en active Pending
Cited By (11)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007072690A1 (en) * | 2005-12-22 | 2007-06-28 | Cataler Corporation | Catalyst for exhaust gas clean-up |
JP2007167780A (en) * | 2005-12-22 | 2007-07-05 | Cataler Corp | Catalyst for exhaust gas purification |
US7956005B2 (en) | 2005-12-22 | 2011-06-07 | Cataler Corporation | Exhaust gas-purifying catalyst |
US8187996B2 (en) | 2005-12-22 | 2012-05-29 | Cataler Corporation | Exhaust gas-purifying catalyst |
WO2008004390A1 (en) * | 2006-07-05 | 2008-01-10 | Cataler Corporation | Catalyst for purifying exhaust gas and process for producing the same |
JP5196656B2 (en) * | 2006-07-05 | 2013-05-15 | 株式会社キャタラー | Exhaust gas purification catalyst and method for producing the same |
US9073048B2 (en) | 2006-07-05 | 2015-07-07 | Cataler Corporation | Exhaust gas-purifying catalyst and method of manufacturing the same |
JP2020513295A (en) * | 2016-11-14 | 2020-05-14 | リサーチ トライアングル インスティテュート | Perovskite catalyst and its use |
US11179704B2 (en) * | 2016-11-14 | 2021-11-23 | Research Triangle Institute | Perovskite catalysts and uses thereof |
US20220111366A1 (en) * | 2016-11-14 | 2022-04-14 | Research Triangle Institute | Perovskite catalysts and uses thereof |
US11559793B2 (en) * | 2016-11-14 | 2023-01-24 | Research Triangle Institute | Perovskite catalysts and uses thereof |
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