JPH02277554A - Production of catalytic carrier made of sheet metal - Google Patents
Production of catalytic carrier made of sheet metalInfo
- Publication number
- JPH02277554A JPH02277554A JP1095418A JP9541889A JPH02277554A JP H02277554 A JPH02277554 A JP H02277554A JP 1095418 A JP1095418 A JP 1095418A JP 9541889 A JP9541889 A JP 9541889A JP H02277554 A JPH02277554 A JP H02277554A
- Authority
- JP
- Japan
- Prior art keywords
- foil
- stainless steel
- resistance
- oxidation
- plating
- 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
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野〕
本発明は、自動車排ガス処理触媒用のメタルハニカム状
等の触媒担持用の1板金属製触媒担体の製造方法に関す
る。DETAILED DESCRIPTION OF THE INVENTION (Industrial Application Field) The present invention relates to a method for manufacturing a single-plate metal catalyst carrier for supporting a catalyst such as a metal honeycomb shape for an automobile exhaust gas treatment catalyst.
従来自動車排ガスの浄化処理用として使用される金属製
の触媒コンバーターハニカムは、1200°C程度の高
温にさらされるために、耐高温酸化性が要求される。従
って、触媒担体の母材としては、Cr15〜20%含む
フェライト系ステンレス鋼にAIを5%添加したステン
レス鋼が使われている。このCr及びAl含有のフェラ
イト系ステンレス鋼を、排気ガス圧損低減の点から熱間
圧延及び冷間圧延により約100I#の厚さの箔に加工
する。その上で、第2図に示すように、単位面積当りの
触媒の担持率を高めるために、先ず基材箔1を低酸素雰
囲気下で短時間予備酸化してα−IV、0.の結晶核2
を形成したのち、大気中で温度約900”Cでv′J8
時間をかけて本格的酸化処理(2次酸化)を施して、2
〜3gm長のα−Af2(hのウィスカー層3を生成さ
せる。図示していないがこののちに、ウォッシュコート
と称するγ−A1zO3の超微細粒子を懸濁させたアル
ミナゾルを塗布乾燥し、触媒担持用の比表面積奄大なる
コート層を形成している。Metal catalytic converter honeycombs conventionally used for purifying automobile exhaust gas are required to have high temperature oxidation resistance because they are exposed to high temperatures of about 1200°C. Therefore, as the base material of the catalyst carrier, stainless steel in which 5% AI is added to ferritic stainless steel containing 15 to 20% Cr is used. This ferritic stainless steel containing Cr and Al is processed into a foil having a thickness of about 100 I# by hot rolling and cold rolling from the viewpoint of reducing exhaust gas pressure loss. Then, as shown in FIG. 2, in order to increase the catalyst loading rate per unit area, first, the base foil 1 is pre-oxidized for a short time in a low oxygen atmosphere to give α-IV, 0. crystal nucleus 2
After forming v′J8 at a temperature of about 900”C in the atmosphere,
After a long period of full-scale oxidation treatment (secondary oxidation),
A whisker layer 3 of α-Af2(h) with a length of ~3 gm is generated.Although not shown, after this, an alumina sol in which ultrafine particles of γ-A1zO3 suspended, called a wash coat, is applied and dried to support the catalyst. It forms a coating layer with a large specific surface area.
この2次酸化によりα−八へ□03のウィスカー層3を
生成させるのは、後工程のγ−AEz(hコート層のた
めのアンカー効果を発揮させるためのものである。The reason why the whisker layer 3 of α-8 to □03 is generated by this secondary oxidation is to exhibit an anchor effect for the γ-AEz (h coat layer) in the subsequent process.
担体用の基材となるAl含有のフェライト系ステンレス
鋼は、耐高温酸化性の点から5%もANを含有させてい
るために非常に跪く、約100−のような薄い箔を得る
のが難しく、従って歩留りが低いために基材箔製造費が
高くついている。The Al-containing ferritic stainless steel, which is the base material for the carrier, contains 5% AN for high-temperature oxidation resistance, so it is very difficult to obtain a thin foil of approximately 100%. The manufacturing cost of the base foil is high due to the difficulty and therefore low yield.
また、α−11LChのウィスカー層3を生成させるた
めの2次酸化処理は厳密な温度コントロールを要し、か
つ8時間という長時間を必要とするためコストアンプの
要因になっている。Further, the secondary oxidation treatment for generating the α-11LCh whisker layer 3 requires strict temperature control and takes a long time of 8 hours, which is a factor in increasing the cost.
本発明は、上記従来の方法の問題点を解決する薄板金属
製触媒担体の製造方法を提供しようとするものである。The present invention aims to provide a method for manufacturing a thin metal catalyst carrier that solves the problems of the above-mentioned conventional methods.
本発明の薄板金属製触媒担体の製造方法は、基材として
A2を含有しないか又はAH含有量2%以下のステンレ
ス鋼を用い、該ステンレス鋼を厚さ100−以下の箔に
加工したのち、核種の表面に八2をメツキ被覆し、その
上で陽性酸化処理を行なう。The method for producing a thin metal catalyst carrier of the present invention uses stainless steel that does not contain A2 or has an AH content of 2% or less as a base material, processes the stainless steel into a foil with a thickness of 100 mm or less, and then The surface of the nuclide is plated with 82, and then positive oxidation treatment is performed.
基材として、ANを含有しないか含有しても2%以下の
ステンレス鋼を用いるので、1001以下という厚さに
迄容易に加工することができるので、箔製造コーストが
下がる。また、このステンレス鋼の表面にAlをメツキ
して被覆することにより、耐高温酸化性を付与すること
ができる。更に、箔の表面にメンキされた八2は陽極酸
化処理を施こすことによって、Alメツキ被覆の表面が
ポーラスになり、後工程の7−Al□0.微粒子のコー
ト層のためのアンカー効果を発揮することができる。Since the base material is stainless steel that does not contain AN or contains 2% or less of AN, it can be easily processed to a thickness of 1001 or less, thereby reducing the foil manufacturing cost. Further, by plating and coating the surface of this stainless steel with Al, high temperature oxidation resistance can be imparted. Furthermore, the surface of the foil plated 82 is anodized to make the surface of the Al plating coating porous, and the surface of the 7-Al□0. It can exert an anchor effect for the fine particle coating layer.
本発明を第1図に示す一実施例によって説明する。 The present invention will be explained with reference to an embodiment shown in FIG.
10は5tlS430等のCrを含存し、A1を含有し
ないフェライト系ステンレス鋼箔であり、この箔は熱間
圧延及び冷間圧延により約100−の厚さに圧延されて
製造される。このとき、ステンレス基材中にはAffi
を含有しないので容易に箔に圧延加工することができる
。なお、ステンレス鋼としては、AEが2%以下の含有
率のものであれば加工性も余り損われないので、基材と
して用いることができる。10 is a ferritic stainless steel foil containing Cr and not containing A1, such as 5tlS430, and this foil is produced by hot rolling and cold rolling to a thickness of about 100 mm. At this time, there is Affi in the stainless steel base material.
Since it does not contain , it can be easily rolled into foil. Note that as long as the stainless steel has an AE content of 2% or less, the workability will not be significantly impaired, so it can be used as a base material.
これらのステンレス鋼は既述のように加工性が良好であ
るので、30−以下の厚さ迄にも加工でき、薄肉にする
ことにより、ハニカム状等の触媒コンバーターとして、
ガス排気性能向上、軽量化等の点で効果を発揮する。As mentioned above, these stainless steels have good workability, so they can be processed to a thickness of 30 mm or less, and by making them thinner, they can be used as honeycomb-shaped catalytic converters.
It is effective in improving gas exhaust performance and reducing weight.
次いで、この箔を脱脂洗浄したのち、Alメツキが施さ
れ、その表面にARメツキ層11が形成される。Next, this foil is degreased and cleaned, and then Al plating is applied to form an AR plating layer 11 on its surface.
このANメツキ層11はステンレス鋼母材を高温酸化か
ら保護する役目をするもので、このへEメツキ層の暎厚
としては耐酸化性及び次工程での陽極酸化処理による多
孔性アルミナ層形成の点から0.5〜10、cmが望ま
しい。このような厚さのへ1メンキ法としては、蒸着法
もしくは溶融塩電気メツキ法が密着性の点からも適する
。This AN plating layer 11 serves to protect the stainless steel base material from high-temperature oxidation, and the thickness of the E plating layer is designed to provide oxidation resistance and the formation of a porous alumina layer by anodizing in the next step. A distance of 0.5 to 10 cm from the point is desirable. As a coating method for such a thickness, a vapor deposition method or a molten salt electroplating method is suitable from the viewpoint of adhesion.
以上のように、Alメツキ被覆を施されたステンレス1
1il箔は、次いで陽極酸化処理されてAffiメツキ
層11に多数の細孔12が開けられる。この陽極処理は
、リン酸、硫酸−重クロム酸、蓚酸等の酸液中で電流密
度2〜3 A/dIlz以下で行なわれる。この際、得
られるAtメツキ層11中の細孔12は、孔径約400
人、深さ数−のものが10”/cm”程度の密度で得ら
れ、メツキ層11は非常に多孔性に富んだ状態となる。As mentioned above, stainless steel 1 coated with Al plating
The 1il foil is then anodized to create a number of pores 12 in the Affi plating layer 11. This anodization is carried out in an acid solution such as phosphoric acid, sulfuric acid-dichromic acid, or oxalic acid at a current density of 2 to 3 A/dIlz or less. At this time, the pores 12 in the At plating layer 11 obtained have a pore diameter of about 400
The plating layer 11 has a density of about 10''/cm'' and has a very high porosity.
従って、後に施されるγ−Affixesのコーティン
グに際し、7−AlzO,の微粒子を数多く安定に保持
することができるアンカーとしての効果を著しく発揮す
ることができる。Therefore, when coating with γ-Affixes to be applied later, the effect as an anchor that can stably hold a large number of 7-AlzO fine particles can be significantly exhibited.
なお、触媒担体は、自動車排ガス処理用ハニカム状等の
触媒、燃焼部の壁として用いられる熱交型触媒等に使用
することができる。Note that the catalyst carrier can be used in a honeycomb-shaped catalyst for treating automobile exhaust gas, a heat exchange type catalyst used as a wall of a combustion section, and the like.
〔発明の効果〕
以上説明したように、本発明では、基材としてAIを含
有しないか又はAffi含を量2%以下のステンレス鋼
を用いることによって、厚さ100−以下の箔に容易に
加工することができ、同箔表面に施されたAtメツキ被
覆によって耐高温酸化性が付与することができ、更に、
Atメツキ被覆に陽極酸化を行なうことによってAlメ
ツキ被覆の表面がポーラスとなり、後工程の7−Alt
O,の微粒子のコート層のためのアンカー効果を発揮す
ることができる。[Effects of the Invention] As explained above, in the present invention, by using stainless steel that does not contain AI or has an Affi content of 2% or less as a base material, it can be easily processed into a foil with a thickness of 100 mm or less. The At plating coating applied to the surface of the foil can provide high temperature oxidation resistance, and further,
By anodizing the At plating coating, the surface of the Al plating coating becomes porous, and the 7-Alt coating in the subsequent process
It can exert an anchoring effect for the coating layer of fine particles of O.
従って、本発明によれば、軽量で抵抗が少く、耐高温酸
化性をもつ触媒担体を安価に製造することができる。Therefore, according to the present invention, a catalyst carrier that is lightweight, has low resistance, and has high temperature oxidation resistance can be manufactured at low cost.
第1図は本発明の一実施例の説明図、第2図は従来の1
板金属製触媒担体の製造方法の説明である。
第1図
1・・・AQ5%添加のステンレス鋼箔、3・・・α−
A12osのウィスカー層、10・・・フェライト系ス
テンレス鋼箔、11・・−Alメツキ層、 12
・・・細孔、第2図Fig. 1 is an explanatory diagram of one embodiment of the present invention, and Fig. 2 is an explanatory diagram of an embodiment of the present invention.
This is an explanation of a method for manufacturing a sheet metal catalyst carrier. Fig. 1 1...Stainless steel foil with 5% AQ addition, 3...α-
A12os whisker layer, 10... Ferritic stainless steel foil, 11...-Al plating layer, 12
... Pore, Figure 2
Claims (1)
のステンレス鋼を用い、該ステンレス鋼を厚さ100μ
m以下の箔に加工したのち、該箔の表面にAlをメッキ
被覆し、その上で陽性酸化処理を行なうことを特徴とす
る薄板金属製触媒担体の製造方法。Stainless steel that does not contain Al or has an Al content of 2% or less is used as the base material, and the stainless steel is made to a thickness of 100 μm.
1. A method for producing a thin metal catalyst carrier, which comprises processing the foil into a foil having a diameter of 1.0 m or less, plating the surface of the foil with Al, and then subjecting the foil to positive oxidation treatment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1095418A JPH02277554A (en) | 1989-04-17 | 1989-04-17 | Production of catalytic carrier made of sheet metal |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1095418A JPH02277554A (en) | 1989-04-17 | 1989-04-17 | Production of catalytic carrier made of sheet metal |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH02277554A true JPH02277554A (en) | 1990-11-14 |
Family
ID=14137138
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1095418A Pending JPH02277554A (en) | 1989-04-17 | 1989-04-17 | Production of catalytic carrier made of sheet metal |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH02277554A (en) |
Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6447453A (en) * | 1987-08-18 | 1989-02-21 | Nisshin Steel Co Ltd | Substrate for catalyst carrier having porous alumina layer |
-
1989
- 1989-04-17 JP JP1095418A patent/JPH02277554A/en active Pending
Patent Citations (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6447453A (en) * | 1987-08-18 | 1989-02-21 | Nisshin Steel Co Ltd | Substrate for catalyst carrier having porous alumina layer |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP3309971B2 (en) | Manufacturing method of exhaust gas purifying catalyst | |
| JPH06126192A (en) | Method for producing metal foil coated with oxide | |
| JPS624441A (en) | Production of cordierite ceramic honeycomb catalytic body | |
| EP0348575B1 (en) | Catalyst carriers and a process for producing the same | |
| JP3414794B2 (en) | Catalyst production method | |
| JPH02277554A (en) | Production of catalytic carrier made of sheet metal | |
| JP3953944B2 (en) | Metal foil and honeycomb structure | |
| JP3989228B2 (en) | Method for producing alumina carrier with excellent heat resistance | |
| JPH08332394A (en) | Exhaust gas-cleaning metal carrier catalyst, and its manufacture | |
| JPH0356147A (en) | Preparation of catalyst carrier | |
| JP2731562B2 (en) | Catalyst carrier and method for producing the same | |
| JPH08197B2 (en) | Substrate for catalyst converter | |
| JPH0548294B2 (en) | ||
| JPS62144750A (en) | Preparation of platinum group oxidizing catalyst | |
| JPH0240734B2 (en) | ||
| RU2378051C1 (en) | Method of preparing catalyst | |
| JPS5923861B2 (en) | Catalyst and its manufacturing method | |
| JPS5959247A (en) | Preparation of catalyst and carrier | |
| JPH07289899A (en) | Heat resistant substrate for catalyst body and its production | |
| JPH03284356A (en) | Plane catalytic body and production thereof | |
| JPS63158135A (en) | Preparation of catalyst carrier made of metal | |
| KR100953531B1 (en) | Catalyst production method using stainless steel as a support | |
| JPS6357780A (en) | Production of metallic carrier for exhaust gas cleaning converter | |
| JPS62140643A (en) | Manufacturing method of porous catalyst for exhaust gas purification | |
| RU2307709C1 (en) | Method of production of the platinum catalyst used for purification of the exhaust gases of the internal combustion engines |