JPH0538438A - Catalyst composition - Google Patents
Catalyst compositionInfo
- Publication number
- JPH0538438A JPH0538438A JP3199099A JP19909991A JPH0538438A JP H0538438 A JPH0538438 A JP H0538438A JP 3199099 A JP3199099 A JP 3199099A JP 19909991 A JP19909991 A JP 19909991A JP H0538438 A JPH0538438 A JP H0538438A
- Authority
- JP
- Japan
- Prior art keywords
- oxide
- catalyst composition
- catalyst
- rare earth
- 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 31
- 239000000203 mixture Substances 0.000 title claims abstract description 17
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 claims abstract description 12
- 229910000510 noble metal Inorganic materials 0.000 claims abstract description 10
- WGLPBDUCMAPZCE-UHFFFAOYSA-N Trioxochromium Chemical compound O=[Cr](=O)=O WGLPBDUCMAPZCE-UHFFFAOYSA-N 0.000 claims abstract description 6
- 229910000423 chromium oxide Inorganic materials 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
- 229910052761 rare earth metal Inorganic materials 0.000 claims abstract description 6
- 229910001404 rare earth metal oxide Inorganic materials 0.000 claims abstract description 5
- 239000002131 composite material Substances 0.000 claims description 5
- 239000012298 atmosphere Substances 0.000 abstract description 4
- 230000003197 catalytic effect Effects 0.000 abstract 1
- 230000002829 reductive effect Effects 0.000 abstract 1
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 19
- 229910052763 palladium Inorganic materials 0.000 description 9
- 238000006243 chemical reaction Methods 0.000 description 6
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 4
- 229910002091 carbon monoxide Inorganic materials 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 4
- 239000007789 gas Substances 0.000 description 4
- QTBSBXVTEAMEQO-UHFFFAOYSA-N Acetic acid Chemical compound CC(O)=O QTBSBXVTEAMEQO-UHFFFAOYSA-N 0.000 description 3
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 3
- 229910000420 cerium oxide Inorganic materials 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 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
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- 229910002651 NO3 Inorganic materials 0.000 description 2
- PHFQLYPOURZARY-UHFFFAOYSA-N chromium trinitrate Chemical compound [Cr+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O PHFQLYPOURZARY-UHFFFAOYSA-N 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
- 238000000034 method Methods 0.000 description 2
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- 229910001868 water Inorganic materials 0.000 description 2
- 229910002210 La0.9Ce0.1CoO3 Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 229910052878 cordierite Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- MVFCKEFYUDZOCX-UHFFFAOYSA-N iron(2+);dinitrate Chemical compound [Fe+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MVFCKEFYUDZOCX-UHFFFAOYSA-N 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000012299 nitrogen atmosphere Substances 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
- 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
- 230000036962 time dependent Effects 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, etc., which converts Ox) into water, carbon dioxide 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クロムと酸化ア
ルミニウム、酸化鉄、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, chromium oxide, aluminum oxide, iron oxide, and among noble metals. One or more of.
【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。With the above-mentioned structure, the present invention suppresses grain growth of noble metal and diffusion into the perovskite complex 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100g、
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(N
O3 )2 〕4.5g、硝酸クロム〔Cr(NO3 )3 〕
5.8g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・5SiO
2 ・2Al2 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
後担体を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2.4
0重量%、パラジウムは0.27重量%、酸化鉄は0.28
重量%、酸化クロムは0.48%であった。La0.9Ce0.1CoO3Of rare earth elements
100 g of perovskite-type composite oxide powder contained
Cerium oxide (CeO2) Powder 100 g, aluminazo
50g (acetic acid acidity, solid content 1/10), palladium nitrate
Mu [Pd (NO3)2] 0.9 g and iron nitrate [Fe (N
O3)2] 4.5 g, chromium nitrate [Cr (NO3)3]
Prepare a slurry by mixing 5.8g and 150g of water with stirring.
did. 400 cells with a grid-like cross section in the slurry
(inch)2Cordierite (2MgO / 5SiO)
2・ 2Al2O3) Honeycomb carrier is dipped and pulled up
After that, the excess slurry was blown off by an air stream. That
The post carrier was dried at 200 ° C for 1 hour and baked at 650 ° C for 1 hour.
About 24% by weight of the catalyst composition and about 76% by weight of the carrier.
A catalyst body of was obtained. Where the perovskite in the catalyst composition
Type composite oxide is 47.8% by weight, aluminum oxide is 2.4
0 wt%, palladium 0.27 wt%, iron oxide 0.28
% By weight, and chromium oxide was 0.48%.
【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、及び酸化クロ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 chromium 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) NO 1%, CO 1%, 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と酸化クロム及び、酸
化鉄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 at least one of a perovskite complex oxide containing a rare earth element, a rare earth oxide, aluminum oxide, chromium oxide, iron oxide and a noble metal. Becomes, 500 ℃
It is a catalyst with excellent durability that suppresses grain growth of noble metals and diffusion into the perovskite composite oxide even in the above high temperature atmosphere.
【図1】本発明の一実施例と比較例の触媒性能の耐久性
を示す図である。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 林 俊一 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 Shunichi Hayashi 300, Takatsuka-cho, 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クロ
ム、酸化鉄からなり、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 catalyst composition comprising a perovskite type composite oxide containing a rare earth element, a rare earth oxide, aluminum oxide, chromium oxide and iron oxide, and one or more kinds of noble metals.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3199099A JPH0538438A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3199099A JPH0538438A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0538438A true JPH0538438A (en) | 1993-02-19 |
Family
ID=16402110
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3199099A Pending JPH0538438A (en) | 1991-08-08 | 1991-08-08 | Catalyst composition |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0538438A (en) |
-
1991
- 1991-08-08 JP JP3199099A patent/JPH0538438A/en active Pending
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