JPH0113901B2 - - Google Patents
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- Publication number
- JPH0113901B2 JPH0113901B2 JP55142240A JP14224080A JPH0113901B2 JP H0113901 B2 JPH0113901 B2 JP H0113901B2 JP 55142240 A JP55142240 A JP 55142240A JP 14224080 A JP14224080 A JP 14224080A JP H0113901 B2 JPH0113901 B2 JP H0113901B2
- Authority
- JP
- Japan
- Prior art keywords
- type
- layer
- metal substrate
- metal
- oxide layer
- 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
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- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Description
本発明は、活性アルミナと貴金属とよりなる触
媒成分をその表面上にコーテイングして支持する
モノリス触媒の金属製担体の改良に関するもので
ある。
自動車エンジン等の排気ガスの浄化用触媒とし
ては、活性アルミナと貴金属とよりなる触媒成分
を担体表面上にコーテイングしたいわゆるモノリ
ス触媒が汎用されている。
従来のモノリス触媒の担体としては、触媒成分
に対する担持性(耐剥離性)に優れたコージライ
トと呼ばれるセラミツクの押出成形品が汎用され
ているが、この種のセラミツク体は、それ自体の
強度が不足し、耐久性に劣るという欠点があつ
た。
これに代る担体として、金属性基体の表面にア
ルミナ層を形成し、このアルミナ層上に、触媒成
分をコーテイングするようにした金属性担体が提
案(例えば、特公昭59−32183号公報参照)され
ているが、かかる金属性担体では、アルミナ層自
体が金属性基体から剥離しやすく、したがつて、
強度的には問題はないが、触媒成分の担持能力に
おいてなお不足し、実用に供しがたい問題があつ
た。
本発明は、かかる従来の問題に鑑みてなされた
ものであつて、金属基体とアルミナ層との結合強
度を向上させ、よつて高い担体能力を示すモノリ
ス触媒の金属製担体を提供することを目的として
いる。
本発明に係る金属製担体は、Cr10〜25%、Al2
〜5%、C0.04%以下、N0.005〜0.05%、Ti0.1〜
0.6%、Zr0.01〜0.5%残部Feで、かつ(Ti+
Zr)/Nの値が10〜150の組成からなる金属基体
の表面に、Ti、Zrを固溶および/または酸化物
の形で含み、α−Al2O3を主成分とする酸化物層
を形成したものであつて、この酸化物層は金属基
体内にくさび状に喰い込んだ状態で金属基体と強
固かつ緻密に結合しており、剥離を生ずることな
く、コーテイングされる触媒成分を担持すること
ができる。
本発明にかかるモノリス触媒の金属製担体は、
上記組成の金属基体を、1000〜1400℃好ましくは
1300℃程度の酸化性雰囲気中で適当な時間、例え
ば、大気中では約2時間かそれ以上の時間加熱
し、所定の加熱後は炉冷または空中放冷すること
によつて得られる。
加熱温度は、1000℃以上でないと、Fe−Cr−
Al系合金の優れた耐酸化性のために所望の酸化
物層を得ることができず、1400℃以上では金属基
体そのものが劣化するので好ましくない。なお、
加熱時間は、雰囲気中の酸素ポテンシヤルや、必
要とされる層厚に応じて適宜決めればよい。
ここに金属基体の組成を限定した理由は下記の
とおりである。Crは耐酸化性付与のため必要不
可欠な成分であり、10%未満では耐酸化性が不十
分となり、25%を超えると加工性が悪化するの
で、10〜25%が適当であり20%程度が最も好まし
い。またAlも高温耐酸化性付与のために不可欠
であり2%未満では耐酸化性が不十分となること
は勿論、酸化被膜に占めるα−Al2O3分を多く
し、かつ(Fe、Cr)2O3などの耐酸化性および耐
食性が劣る酸化物の生成をできるだけ少量に抑え
るために、最低2%は必要であり、5%を超える
とCr同様常温加工性が劣化するので、2〜5%
を適当とし3%内外が最適である。なお、Crお
よびAlは従来のFe−Cr−Al系電熱合金における
同じく、酸化被膜よりも金属基体そのものの高温
繰返し加熱に対するクリープ抵抗および耐酸化性
を増加させるためであり、添加量も従来品と大同
小異である。
CはTi、Zr、Cr等と基地に固溶しない炭化物
を生成し、これら炭化物が多く生成されること粒
界破断の原因となるばかりでなく、酸化被膜強化
のために添加するTiおよびZrの効果を減ずるの
で、できるだけ少量であることが望ましくその許
容範囲は0.04%以下である。
NはCの拡散を抑え炭化物の粒子の粗大化を防
止するが、CよりもTi、Zrとの親和力が強く窒
化物TiN、ZrNを生成し、C以上にTiおよびZr
の効果を減ずるのでできるだけ少量であることが
望ましく、その上限は0.05%である。またNは後
述するように(Ti+Zr)/Nの値を指針として
酸化被膜の諸性質に影響を与えると考えられるの
で、この観点から下限を0.005%とした。
TiおよびZrの添加は、既に述べたように、高
温に加熱した時その拡散挙動によつて耐剥離性被
膜を金属基体の表面に緻密強固に形成するためで
ある。Tiはα−Al2O3に固溶し酸化被膜自体を緻
密にするものであり、0.1%以下では著効がなく
他方0.6%以上では常温加工性が困難となるので、
0.1〜0.6%が適当である。ZrはNを固定してTiの
効果を上げるとともに酸化被膜の耐剥離性を向上
させ、さらにはTiと同様にα−Al2O3に固溶し酸
化物の緻密化に寄与するもので、Nを固定する見
地から少くとも0.01%は必要であるが0.5%を超
えると耐酸化性が大巾に低下するので、0.01%〜
0.5%が適当である。
(Ti+Zr)/Nの値(重量%比)は熱処理に
おける酸化物層の生成および耐剥離性にとつて重
要なパラメータであつて、10以下でも150以上で
も必要な耐剥離性が得られない。
第1図A〜Eに図式化して示すように、上記の
値(Ti+Zr)/Nを種々変えると、熱処理によ
つて生成される酸化物層および金属基体との結合
状態は種々変化する。
第1図Aに示すA型は、金属基体とZrO2が拡
散したα−Al2O3層とが比較的なだらかな凹凸面
によつて結合され、α−Al2O3層のうえには、
Al2O3とTiO2とが相溶した薄膜が生成されたもの
である。
第1図Bに示すB型は、金属基体とZrO2が拡
散したα−Al2O3とが、複数に入り組んだ状態で
結合されており、第1図Cに示すC型はB型と同
様のα−Al2O3層のうえに(Fe、Cr)2O3薄膜が形
成され、さらに第1図Dに示すD型はC型に比し
てα−Al2O3層が若干薄くなり、α−Al2O3層と
(Fe、Cr)2O3層との境界がゆるやかな凹凸をな
し、(Fe、Cr)2O3層中にはZrO2が拡散した状態
となる。
さらに、第1図Eに示すE型では、金属基体と
α−Al2O3層とが、A型と同様、ゆるやかな凹凸
面をなして結合され、α−Al2O3層が薄くなり、
逆にZrO2が拡散した(Fe、Cr)2O3層の厚みが増
大する。
これらの結合状態のうち、A型およびE型は、
金属基体とα−Al2O3を主成分とする酸化物層と
がゆるやかな凹凸面で結合されているのに対し、
B型、C型およびD型は金属基体と酸化物層とが
複雑に入り組んだかたちで結合されており、A型
又はE型に比して格段に結合性、密着性が優れて
いるものと考えられる。
これらA型〜E型について行なつた密着性試験
の測定結果を以下の表に示すように、事実、B
型、C型、D型はA型、E型に比して、優れた耐
剥離性を示す。密着性試験は、テスト試料30mm×
10mm×2mmを1300℃で20時間加熱したのち、サン
ドブラストを5分間吹付けることにより行ない、
その場合の酸化増量と剥離量とを測定した。
The present invention relates to an improvement in a metal carrier for a monolithic catalyst, which supports a catalyst component consisting of activated alumina and a noble metal by coating it on its surface. As catalysts for purifying exhaust gas from automobile engines, etc., so-called monolith catalysts, in which catalyst components consisting of activated alumina and precious metals are coated on the surface of a carrier, are widely used. Conventional carriers for monolithic catalysts are commonly extruded ceramic products called cordierite, which have excellent support for catalyst components (peel resistance); however, this type of ceramic body lacks its own strength. It had the disadvantage of being insufficient and having poor durability. As an alternative carrier, a metallic carrier has been proposed in which an alumina layer is formed on the surface of a metallic substrate and a catalyst component is coated on this alumina layer (for example, see Japanese Patent Publication No. 59-32183). However, in such metallic carriers, the alumina layer itself tends to peel off from the metallic substrate, and therefore,
Although there was no problem in terms of strength, the ability to support catalyst components was still insufficient, making it difficult to put it to practical use. The present invention has been made in view of such conventional problems, and an object of the present invention is to provide a metal carrier for a monolith catalyst that improves the bonding strength between the metal substrate and the alumina layer and exhibits higher support capacity. It is said that The metal carrier according to the present invention contains 10 to 25% Cr, Al2
~5%, C0.04% or less, N0.005~0.05%, Ti0.1~
0.6%, Zr0.01~0.5% balance Fe, and (Ti+
An oxide layer containing Ti and Zr in solid solution and/or oxide form and mainly composed of α-Al 2 O 3 on the surface of a metal substrate having a composition with a Zr)/N value of 10 to 150. This oxide layer is wedged into the metal substrate and is strongly and densely bonded to the metal substrate, supporting the catalyst component to be coated without peeling. can do. The metal carrier of the monolithic catalyst according to the present invention is
A metal substrate having the above composition is heated preferably at 1000 to 1400℃.
It can be obtained by heating in an oxidizing atmosphere at about 1300° C. for an appropriate time, for example, about 2 hours or more in the air, and after the prescribed heating, cooling in a furnace or cooling in the air. If the heating temperature is not above 1000℃, Fe−Cr−
Due to the excellent oxidation resistance of Al-based alloys, it is not possible to obtain a desired oxide layer, and temperatures above 1400°C are undesirable because the metal substrate itself deteriorates. In addition,
The heating time may be appropriately determined depending on the oxygen potential in the atmosphere and the required layer thickness. The reason for limiting the composition of the metal substrate is as follows. Cr is an essential component for imparting oxidation resistance. If it is less than 10%, oxidation resistance will be insufficient, and if it exceeds 25%, workability will deteriorate, so 10 to 25% is appropriate, and about 20%. is most preferred. Al is also essential for imparting high-temperature oxidation resistance, and if it is less than 2 %, the oxidation resistance will of course be insufficient . ) In order to suppress the production of oxides with poor oxidation and corrosion resistance such as 2O3 , a minimum content of 2% is required. 5%
A value of around 3% is optimal. Note that Cr and Al are used to increase the creep resistance and oxidation resistance of the metal base itself against repeated high-temperature heating, rather than the oxide film, as in conventional Fe-Cr-Al electrothermal alloys, and the amounts added are also different from those of conventional products. They are the same and the same. C forms carbides that do not dissolve in the matrix with Ti, Zr, Cr, etc., and the generation of a large amount of these carbides not only causes grain boundary fracture, but also increases the amount of Ti and Zr added to strengthen the oxide film. Since it reduces the effect, it is desirable to keep the amount as small as possible, and the allowable range is 0.04% or less. N suppresses the diffusion of C and prevents the coarsening of carbide particles, but it has a stronger affinity with Ti and Zr than C, forming nitrides TiN and ZrN, and it has a stronger affinity with Ti and Zr than with C.
It is desirable to keep the amount as small as possible, as it reduces the effect of , and the upper limit is 0.05%. Further, as will be described later, since it is thought that N influences various properties of the oxide film using the value of (Ti+Zr)/N as a guideline, the lower limit was set at 0.005% from this viewpoint. As already mentioned, Ti and Zr are added to form a dense and strong peel-resistant coating on the surface of the metal substrate by their diffusion behavior when heated to high temperatures. Ti dissolves in α-Al 2 O 3 and makes the oxide film itself dense, and if it is less than 0.1%, it has no significant effect, while if it is more than 0.6%, it becomes difficult to work at room temperature.
0.1-0.6% is appropriate. Zr fixes N, improves the effectiveness of Ti, and improves the peeling resistance of the oxide film. Furthermore, like Ti, Zr dissolves in α-Al 2 O 3 and contributes to the densification of the oxide. From the standpoint of fixing N, at least 0.01% is necessary, but if it exceeds 0.5%, the oxidation resistance will decrease significantly, so 0.01%~
0.5% is appropriate. The value of (Ti+Zr)/N (weight % ratio) is an important parameter for the formation of an oxide layer during heat treatment and peeling resistance, and if it is less than 10 or more than 150, the necessary peeling resistance cannot be obtained. As schematically shown in FIGS. 1A to 1E, when the above value (Ti+Zr)/N is varied, the bonding state between the oxide layer produced by the heat treatment and the metal substrate changes in various ways. In type A shown in Fig. 1A, the metal substrate and the α-Al 2 O 3 layer in which ZrO 2 is diffused are bonded by a relatively smooth uneven surface, and the α-Al 2 O 3 layer is ,
A thin film is produced in which Al 2 O 3 and TiO 2 are compatible. Type B shown in Figure 1B has a metal base and α-Al 2 O 3 in which ZrO 2 has been diffused, bonded in a complicated manner, and Type C shown in Figure 1C is different from Type B. A (Fe, Cr) 2 O 3 thin film is formed on a similar α-Al 2 O 3 layer, and the α-Al 2 O 3 layer is slightly smaller in the D type shown in Figure 1 D than in the C type. It becomes thinner, the boundary between the α-Al 2 O 3 layer and the (Fe, Cr) 2 O 3 layer becomes gently uneven, and ZrO 2 becomes diffused in the (Fe, Cr) 2 O 3 layer. . Furthermore, in the E type shown in Figure 1E, the metal substrate and the α-Al 2 O 3 layer are bonded with a gently uneven surface, similar to the A type, and the α-Al 2 O 3 layer becomes thinner. ,
Conversely, the thickness of the (Fe, Cr) 2 O 3 layer in which ZrO 2 is diffused increases. Among these bonding states, type A and type E are
While the metal substrate and the oxide layer mainly composed of α-Al 2 O 3 are bonded by a gently uneven surface,
Types B, C, and D have a metal base and oxide layer bonded in a complicated manner, and have much better bonding and adhesion than types A or E. Conceivable. As shown in the table below, the measurement results of the adhesion tests conducted on these types A to E indicate that in fact, B
Types C, C, and D exhibit superior peeling resistance compared to A and E types. For adhesion test, test sample 30mm x
After heating 10mm x 2mm at 1300℃ for 20 hours, sandblasting was performed for 5 minutes.
The oxidation weight gain and peeling amount in that case were measured.
【表】
この表から明らかなように、B型、C型および
D型は、A型、E型および参考のため作成した
Fe−Cr−Al−Y合金サンプルに比して格段に優
れた耐剥離性を示す。
また、第2図にZr量および(Ti+Zr)/Nの
値を種々変化させたときのA〜E型酸化物層の形
成範囲を示す。
第2図から明らかなように、A型は他の型に比
して(Ti+Zr)/Nが相対的に小さい領域で形
成される一方、E型は他の型に比して(Ti+
Zr)/NおよびZr量が多い領域において形成さ
れ、B型、C型、D型は、A型とE型の中間の領
域に形成される。
上記の如き、A型〜E型の生成機構は、必らず
しも明らかではないが、金属基体中の合金元素の
拡散速度、酸素との親和力、さらには、上記
(Ti+Zr)/Nの値等が、複雑に相関した結果で
あると考えられる。
上記の如き組成を有する金属基体は、予じめモ
ノリス触媒として最適な形状に成形加工したうえ
で熱処理することにより、上記の如きB型、C
型、もしくはD型の酸化物層を形成し、このよう
にして得た金属製担体には、デイツピング等によ
り、γ−Al2O3と貴金属よりなる触媒成分をコー
テイングするようにすればよい。
このようにして得たモノリス触媒は、触媒成分
の担持体である酸化物層が金属基体に強固、緻密
に結合されているため、高温の排気ガスにさらさ
れ、しかも種々の振動を受けたとしても、剥離を
生ずることなく触媒成分を担持することができ、
その担持能力を著しく向上させることができ、強
度的に有利である金属製担体の実用化に大きく貢
献することができる。[Table] As is clear from this table, type B, type C, and type D were created for reference as well as type A, E.
It exhibits much superior peeling resistance compared to the Fe-Cr-Al-Y alloy sample. Further, FIG. 2 shows the formation range of A to E type oxide layers when the Zr amount and the value of (Ti+Zr)/N were varied. As is clear from Figure 2, type A is formed in a region where (Ti+Zr)/N is relatively small compared to other types, while type E is formed in a region where (Ti+Zr)/N is relatively small compared to other types.
Type B, type C, and type D are formed in a region intermediate between type A and type E. The formation mechanism of types A to E as described above is not necessarily clear, but it depends on the diffusion rate of the alloying element in the metal substrate, the affinity with oxygen, and the value of (Ti+Zr)/N mentioned above. This is thought to be the result of a complex interrelationship. The metal substrate having the composition as described above is molded in advance into an optimal shape as a monolith catalyst and then heat-treated to form a B-type, C-type as described above.
A type or D-type oxide layer may be formed, and the metal carrier thus obtained may be coated with a catalyst component consisting of γ-Al 2 O 3 and a noble metal by dipping or the like. The monolithic catalyst obtained in this way has an oxide layer, which is a support for catalyst components, firmly and densely bonded to a metal substrate, so it is exposed to high-temperature exhaust gas and subjected to various vibrations. can also support catalyst components without causing peeling,
The supporting capacity can be significantly improved, and it can greatly contribute to the practical application of metal carriers that are advantageous in terms of strength.
第1図A,B,C,D,Eは各々金属基体とそ
の上に形成される酸化物層の組織状態を図式化し
て示す拡大断面説明図、第2図はZr量を横軸に、
(Ti+Zr)/Nを縦軸として第1図A〜Eに示す
酸化物層の生成領域を示すグラフである。
Figures 1A, B, C, D, and E are enlarged cross-sectional explanatory diagrams schematically showing the structure of the metal substrate and the oxide layer formed thereon, and Figure 2 shows the amount of Zr on the horizontal axis.
2 is a graph showing the formation region of the oxide layer shown in FIGS. 1A to 1E with (Ti+Zr)/N as the vertical axis.
Claims (1)
N0.005〜0.05%、Ti0.1〜0.6%、Zr0.01〜0.5%、
残部Feで、かつ、(Ti+Zr)/Nの値が10〜150
の組成からなる金属基体の表面に、Ti、Zrを固
溶および/または酸化物の形で含むα−Al2O3の
酸化物層を形成してなり、該酸化物層の表面に活
性アルミナと貴金属とよりなる触媒成分をコーテ
イングするようにしたモノリス触媒の金属製担
体。1 Cr10~25%, Al2~5%, C0.04% or less,
N0.005~0.05%, Ti0.1~0.6%, Zr0.01~0.5%,
The remainder is Fe, and the value of (Ti+Zr)/N is 10 to 150
An oxide layer of α-Al 2 O 3 containing Ti and Zr in solid solution and/or oxide form is formed on the surface of a metal substrate having a composition of A monolithic catalyst metal carrier coated with a catalyst component consisting of precious metals and precious metals.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55142240A JPS5768143A (en) | 1980-10-11 | 1980-10-11 | Carrier made of metal for monolithic catalyst |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55142240A JPS5768143A (en) | 1980-10-11 | 1980-10-11 | Carrier made of metal for monolithic catalyst |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5768143A JPS5768143A (en) | 1982-04-26 |
| JPH0113901B2 true JPH0113901B2 (en) | 1989-03-08 |
Family
ID=15310687
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55142240A Granted JPS5768143A (en) | 1980-10-11 | 1980-10-11 | Carrier made of metal for monolithic catalyst |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5768143A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006110485A (en) * | 2004-10-15 | 2006-04-27 | Johnson Matthey Japan Inc | Exhaust gas catalyst and exhaust gas trteatment apparatus using the catalyst |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH067922B2 (en) * | 1987-07-09 | 1994-02-02 | トヨタ自動車株式会社 | Exhaust gas purification catalyst |
| JPH02194842A (en) * | 1989-01-20 | 1990-08-01 | Toyota Motor Corp | Catalyst for purifying exhaust gas |
| JP2007275704A (en) * | 2006-04-03 | 2007-10-25 | Johnson Matthey Japan Inc | Exhaust gas catalyst and exhaust gas treating device using the same |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5028409A (en) * | 1973-07-17 | 1975-03-24 | ||
| JPS5140318A (en) * | 1974-10-03 | 1976-04-05 | Tokyo Shibaura Electric Co | KINZOKUSHIIZUKOTAI |
| SE422744B (en) * | 1975-08-20 | 1982-03-29 | Atomic Energy Authority Uk | CATALYST BODY WITH CONTINUOUS CHANNELS AS SET FOR ITS MANUFACTURING |
-
1980
- 1980-10-11 JP JP55142240A patent/JPS5768143A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2006110485A (en) * | 2004-10-15 | 2006-04-27 | Johnson Matthey Japan Inc | Exhaust gas catalyst and exhaust gas trteatment apparatus using the catalyst |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5768143A (en) | 1982-04-26 |
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