JPH10365A - Catalyst carrier and method for producing the same - Google Patents

Catalyst carrier and method for producing the same

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Publication number
JPH10365A
JPH10365A JP8158481A JP15848196A JPH10365A JP H10365 A JPH10365 A JP H10365A JP 8158481 A JP8158481 A JP 8158481A JP 15848196 A JP15848196 A JP 15848196A JP H10365 A JPH10365 A JP H10365A
Authority
JP
Japan
Prior art keywords
catalyst carrier
metal foil
catalyst
metal
foil body
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
Application number
JP8158481A
Other languages
Japanese (ja)
Inventor
Kunio Kimura
邦夫 木村
Tetsuo Terajima
徹生 寺島
Kiyoshi Taguchi
清 田口
Yoshitaka Kawasaki
良隆 川崎
Masato Hosaka
正人 保坂
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP8158481A priority Critical patent/JPH10365A/en
Publication of JPH10365A publication Critical patent/JPH10365A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】 【課題】 熱伝導性や耐熱衝撃性に優れた金属製の触媒
担体を、廉価で提供する。 【解決手段】 表面に複数個の凸部を備えた金属箔体
を、金属箔体の平坦部が相互に密着しないように捲回し
た円柱状の捲回体を具備する。
(57) [Problem] To provide an inexpensive metal catalyst carrier having excellent thermal conductivity and thermal shock resistance. SOLUTION: There is provided a columnar winding body formed by winding a metal foil body having a plurality of convex portions on the surface so that flat portions of the metal foil body do not adhere to each other.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、排ガス浄化や、燃
焼などに用いる触媒部材の金属製のハニカム状触媒担体
およびその製造法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a honeycomb catalyst carrier made of metal for a catalyst member used for exhaust gas purification, combustion and the like, and a method for producing the same.

【0002】[0002]

【従来の技術】触媒部材には、主としてハニカム状の触
媒担体に貴金属等の触媒を担持させたものが用いられ
る。触媒を担持させるハニカム状触媒担体は、大きくセ
ラミックス製と金属製に分類される。セラミックス製の
触媒担体としては、コージェライト、シリカ−アルミ
ナ、SiCなどからなるものが挙げられるが、このうち
最もよく用いられているのがコージェライト製のもので
ある。コージェライトは、耐熱性に優れており、また、
種々のセル数を持った任意の形状のものを連続的に成形
可能であることから、廉価に製造することができるた
め、自動車の排ガス浄化用の触媒部材の触媒担体とし
て、広く用いられている。しかし、熱伝導性は金属製の
ハニカム状触媒担体に劣り、また熱衝撃により亀裂が生
じやすいといった問題点がある。一方、金属製のハニカ
ム状触媒担体は、熱伝導性、耐熱衝撃性、機械的強度等
に優れるといった利点を有するものの、価格的に高価な
ため、これまで広く普及するには至っていなかった。
2. Description of the Related Art As a catalyst member, a honeycomb-shaped catalyst carrier having a catalyst such as a noble metal supported thereon is used. Honeycomb-shaped catalyst carriers for supporting a catalyst are roughly classified into ceramic and metal. Examples of the ceramic catalyst carrier include cordierite, silica-alumina, and SiC. Among them, cordierite is most frequently used. Cordierite has excellent heat resistance,
Since it can be continuously molded into any shape having various numbers of cells, it can be manufactured at low cost, and is widely used as a catalyst carrier for a catalyst member for purifying exhaust gas from automobiles. . However, there is a problem that the thermal conductivity is inferior to that of a metal honeycomb catalyst carrier, and cracks are easily generated by thermal shock. On the other hand, honeycomb catalyst carriers made of metal have advantages such as excellent thermal conductivity, thermal shock resistance, and mechanical strength, but have not been widely used because of their high price.

【0003】[0003]

【発明が解決しようとする課題】金属製のハニカム状触
媒担体が価格的に高価な理由は、波状と板状の金属箔を
交互に配設し、部分的に溶接するといった工程で製造す
るため、製造が非常に煩雑であることによる。本発明
は、金属製のハニカム状触媒担体を、一枚の金属箔体か
ら連続的に製造することにより、廉価に提供することを
目的とする。
The reason why the metallic honeycomb-shaped catalyst carrier is expensive is that it is manufactured by a process in which corrugated and plate-shaped metal foils are alternately arranged and partially welded. , Because the production is very complicated. An object of the present invention is to provide a honeycomb catalyst carrier made of metal at a low cost by continuously manufacturing the same from a single metal foil body.

【0004】[0004]

【課題を解決するための手段】本発明の金属製のハニカ
ム状触媒担体は、表面に複数個の凸部を設けた金属箔体
を、その平坦部が相互に密着しないように複数の凸部を
分散配置させて捲回し、その外周部をスポット溶接など
により接着して所望の形状に成形するものである。本発
明によると、連続的に成形可能である。さらに触媒担体
の圧力損失を、形成する凸部の数や形状等によって容易
に調整することができる。
According to the present invention, there is provided a metal honeycomb catalyst carrier comprising a plurality of convex portions provided on a surface thereof, the plurality of convex portions being provided so that the flat portions do not adhere to each other. Are wound in a dispersed arrangement, and the outer periphery thereof is bonded by spot welding or the like to form a desired shape. According to the present invention, continuous molding is possible. Further, the pressure loss of the catalyst carrier can be easily adjusted by the number and shape of the projections to be formed.

【0005】[0005]

【発明の実施の形態】本発明の触媒担体は、表面に複数
個の凸部を備えた金属箔体を金属箔体の平坦部が相互に
密着しないように捲回した円柱状の捲回体を具備するも
のである。凸部は、エンボス加工等により、金属箔体表
面に半球状、角錐状等の突起として形成してもよく、あ
るいは金属箔体自体を、矩形状、波形状等に加工して形
成してもよい。金属箔体の平坦部を相互に密着させない
ための具体的な手段としては、凸部の配置に規則性を持
たせないことが効果的である。これにより、一カ所が密
着しても、他の箇所で隙間を形成することができる。規
則性を持たせた場合には、捲回時に平坦部同士が密着し
ない箇所に凸部を設ける必要がある。
BEST MODE FOR CARRYING OUT THE INVENTION A catalyst support of the present invention is a cylindrical rolled body obtained by winding a metal foil having a plurality of convex portions on its surface so that flat portions of the metal foil do not adhere to each other. It is provided with. The convex portion may be formed as a hemisphere, a pyramid-shaped projection, or the like on the surface of the metal foil body by embossing or the like, or may be formed by processing the metal foil body itself into a rectangular shape, a wavy shape, or the like. Good. As a specific means for preventing the flat portions of the metal foil body from adhering to each other, it is effective that the arrangement of the convex portions does not have regularity. Thus, even if one place is in close contact, a gap can be formed in another place. In the case where regularity is provided, it is necessary to provide a convex portion at a position where flat portions do not adhere to each other during winding.

【0006】また、捲回体の外周側面に内接して配され
た筒状の金属部材を具備することが好ましい。筒状の金
属部材の内部に前述の円柱状捲回体を挿入することによ
り、円柱状捲回体の外周側端部をその内側表面に対向す
る面に接着して、捲回体の形状を固定する必要がなくな
る。さらに、金属部材の両端の開口部に滑りどめ用の爪
などを設けることにより、捲回体が作動中に移動して脱
離することを防止できる。また、筒状金属部材の形状
は、円筒に限るものではなく、多角柱状であってもよ
い。
[0006] It is preferable that a cylindrical metal member is provided so as to be inscribed on the outer peripheral side surface of the wound body. By inserting the above-mentioned cylindrical wound body into the inside of the cylindrical metal member, the outer peripheral end of the cylindrical wound body is bonded to the surface facing the inner surface, and the shape of the wound body is reduced. There is no need to fix. Further, by providing the sliding members with claws or the like at the openings at both ends of the metal member, it is possible to prevent the wound body from moving during operation and coming off. Further, the shape of the cylindrical metal member is not limited to a cylinder, but may be a polygonal column.

【0007】さらに、凸部が部分的に裂孔を有すること
が好ましい。この場合、触媒担体に流入するガスが、裂
孔により乱流になるため、ガスと触媒の接触の機会が多
くなる。また、触媒担体の表面積が増大することによ
り、浄化能は向上する。
[0007] Further, it is preferable that the convex portion has a partially broken hole. In this case, the gas flowing into the catalyst carrier becomes turbulent due to the cracks, so that the chance of contact between the gas and the catalyst increases. Further, the purifying ability is improved by increasing the surface area of the catalyst carrier.

【0008】また、金属箔体が、Alを含むステンレス
鋼からなることが好ましい。触媒担体として用いる金属
材料としては、耐食性を有していることが必要である。
特に、Alを含むステンレス鋼は、耐熱性に優れている
こと、さらに熱処理によって成分中のAlが繊維状のA
23を形成し、これが触媒の担持に効果的であること
から好ましい。
It is preferable that the metal foil is made of stainless steel containing Al. It is necessary that the metal material used as the catalyst carrier has corrosion resistance.
In particular, stainless steel containing Al is excellent in heat resistance, and furthermore, the Al in the component becomes fibrous A by heat treatment.
It forms l 2 O 3 , which is preferred because it is effective for supporting the catalyst.

【0009】本発明の触媒担体の製造法は、表面に複数
個の凸部を備えた金属箔体の端部を、棒状または筒状の
金属部材に接着したのち、前記芯材を中心軸として、前
記金属箔体を、平坦部が相互に密着しないように円柱状
に捲回するものである。金属箔体の一端を棒状もしくは
筒状の芯材にスポット溶接機などを用いて接着してか
ら、箔体を捲回することにより、精度よく捲回すること
ができる。
In the method for producing a catalyst carrier according to the present invention, the end of a metal foil having a plurality of projections on its surface is bonded to a rod-shaped or cylindrical metal member, and then the core material is used as a center axis. The metal foil body is wound in a cylindrical shape so that the flat portions do not adhere to each other. By bonding one end of the metal foil body to a rod-shaped or cylindrical core material using a spot welding machine or the like, and then winding the foil body, accurate winding can be achieved.

【0010】[0010]

【実施例】以下、本発明の実施例を図面を用いて詳細に
説明する。
Embodiments of the present invention will be described below in detail with reference to the drawings.

【0011】《実施例1》長さ200mm、幅20mm
で厚さ50ミクロンのステンレス鋼(70wt%Fe−
25wt%Cr−5wt%Al)製の金属箔体1に、プ
レスにより、図1に示すように複数の略半球状の凸部3
を一定方向に形成した。この凸部3は、球の直径の平均
が3mm、山の高さの平均が2.5mmであり、金属箔
体1表面に92個形成した。ただし、金属箔体1の長さ
方向の端部には凸部を設けていない。この金属箔体1
を、図2に示すように、長さ方向に捲回した後、外周側
の端部を、スポット溶接により内接する金属箔体1の平
坦部2に接着し、直径が50mmで、高さが20mmの
円柱状の捲回体を得た。この捲回体を1000℃で3時
間熱処理し、表面に酸化皮膜を形成した。さらに、この
捲回体を、水酸化アルミニウムおよび酸化バリウムを水
に分散させたスラリーに浸漬し、その後500℃で1時
間熱処理を行うことにより、捲回体表面に耐食層を形成
して触媒担体を得た。
Example 1 Length 200 mm, width 20 mm
Stainless steel (70 wt% Fe-
As shown in FIG. 1, a plurality of substantially hemispherical projections 3 are formed on a metal foil body 1 made of 25 wt% Cr-5 wt% Al) by pressing.
Was formed in a certain direction. The projections 3 had an average diameter of the sphere of 3 mm and an average height of the ridge of 2.5 mm, and were formed on the surface of the metal foil body 1 in 92 pieces. However, no protrusion is provided at the end in the length direction of the metal foil body 1. This metal foil 1
As shown in FIG. 2, after being wound in the length direction, the end on the outer peripheral side is bonded to the flat portion 2 of the metal foil body 1 inscribed by spot welding, and has a diameter of 50 mm and a height of 50 mm. A cylindrical wound body of 20 mm was obtained. This wound body was heat-treated at 1000 ° C. for 3 hours to form an oxide film on the surface. Further, this wound body is immersed in a slurry in which aluminum hydroxide and barium oxide are dispersed in water, and then subjected to a heat treatment at 500 ° C. for 1 hour to form a corrosion-resistant layer on the surface of the wound body and form a catalyst carrier. I got

【0012】次に、この触媒担体をジニトロジアミン白
金水溶液に浸漬し、乾燥した後、500℃で3時間熱処
理して、表面にPtを担持した触媒体を得た。この触媒
体を石英管中に設置し、石英管にイソブタン1000p
pmを含む空気を空間速度10000[h-1]で流通さ
せた。このときの触媒体の前後のイソブタン濃度をガス
クロマトグラフィを用いて測定し、これより、触媒体の
イソブタンの転換率を求めた。その結果、環境温度20
0℃で70%、250℃で100%であった。
Next, this catalyst carrier was immersed in an aqueous solution of dinitrodiamine platinum, dried, and then heat-treated at 500 ° C. for 3 hours to obtain a catalyst having Pt supported on the surface. This catalyst was placed in a quartz tube, and isobutane 1000 p
The air containing pm was flowed at a space velocity of 10,000 [h -1 ]. At this time, the isobutane concentrations before and after the catalyst body were measured using gas chromatography, and the conversion rate of isobutane of the catalyst body was determined from this. As a result, the environmental temperature 20
70% at 0 ° C and 100% at 250 ° C.

【0013】《実施例2》長さ250mm、幅20mm
で厚さ50ミクロンのステンレス鋼(70wt%Fe−
25wt%Cr−5wt%Al)製の金属箔体11を、
図3に示すように、幅方向に連なる高さ2.0mm、幅
2.0mmの山13を複数備えた矩形状に加工し、これ
を用いて実施例1と同様に、直径が50mmで、高さが
20mmの円柱状の触媒体を作製した。得られた触媒体
について、実施例1と同様にイソブタンの転換率を求め
た結果、環境温度200℃で68%、250℃で98%
であった。
<< Embodiment 2 >> Length 250 mm, width 20 mm
Stainless steel (70 wt% Fe-
A metal foil body 11 made of 25 wt% Cr-5 wt% Al)
As shown in FIG. 3, a rectangular shape having a plurality of peaks 13 each having a height of 2.0 mm and a width of 2.0 mm connected in the width direction is formed. A cylindrical catalyst body having a height of 20 mm was produced. With respect to the obtained catalyst, the conversion of isobutane was determined in the same manner as in Example 1. As a result, 68% at an ambient temperature of 200 ° C. and 98% at an ambient temperature of 250 ° C.
Met.

【0014】《実施例3》実施例1と同様のステンレス
鋼製の金属箔体を、図4に示すように、山の高さが平均
で2.3mmであり、その直径が平均で3mmである凸
部23をプレスにより一定方向に形成した。この凸部2
3は、金属箔体21の表面に74個形成されており、こ
のうち複数の凸部の頂部には、裂孔26を有する。これ
を用いて実施例1と同様に、直径が50mmで、高さが
20mmの円柱状の触媒体を作製した。得られた触媒体
について、実施例1と同様にイソブタンの転換率を求め
た結果、環境温度200℃で75%、250℃で100
%であった。
<< Example 3 >> A stainless steel metal foil body similar to that of Example 1 was used, as shown in FIG. 4, with a peak height of 2.3 mm on average and a diameter of 3 mm on average. A certain convex portion 23 was formed in a certain direction by pressing. This convex part 2
74 are formed on the surface of the metal foil body 21, and among them, the top of the plurality of projections has a crack 26. Using this, a cylindrical catalyst body having a diameter of 50 mm and a height of 20 mm was produced in the same manner as in Example 1. With respect to the obtained catalyst, the conversion of isobutane was determined in the same manner as in Example 1. As a result, 75% at 200 ° C. and 100% at 250 ° C.
%Met.

【0015】《実施例4》実施例2で用いたものと同様
の金属箔体31を、図5に示すように、直径5mm、長
さ20mmのステンレス鋼製の金属棒35に捲回し、さ
らに、これらの外周に直径50mm、長さ20mmの、
ステンレス鋼製の金属円筒36を配置した。得られた触
媒体について、実施例1と同様にイソブタンの転換率を
求めた結果、環境温度200℃で76%、250℃で9
9%であった。
Example 4 A metal foil body 31 similar to that used in Example 2 was wound around a stainless steel metal rod 35 having a diameter of 5 mm and a length of 20 mm as shown in FIG. , 50 mm in diameter and 20 mm in length around these
A metal cylinder 36 made of stainless steel was arranged. With respect to the obtained catalyst, the conversion of isobutane was determined in the same manner as in Example 1. As a result, 76% at 200 ° C. and 9% at 250 ° C.
9%.

【0016】《比較例》市販の金属製ハニカム体を触媒
担体として、実施例1と同様の操作により、触媒体を作
製した。金属製ハニカム体には、直径50mm、厚さ2
0mmの円筒状で、厚さ方向に200セル/平方インチ
の貫通孔を有するコルゲート状のものを用いた。得られ
た触媒体について、実施例1と同様にイソブタンの転換
率を求めた結果、環境温度200℃で71%、250℃
で100%であった。
Comparative Example A catalyst body was prepared in the same manner as in Example 1 using a commercially available metal honeycomb body as a catalyst carrier. The metal honeycomb body has a diameter of 50 mm and a thickness of 2 mm.
A corrugated one having a cylindrical shape of 0 mm and a through hole of 200 cells / square inch in the thickness direction was used. With respect to the obtained catalyst, the conversion of isobutane was determined in the same manner as in Example 1. As a result, 71% at an ambient temperature of 200 ° C. and 250 ° C.
Was 100%.

【0017】以上より、本実施例の金属製触媒担体を用
いた触媒体は、比較例の金属製触媒担体を用いた触媒体
と比べて、ほぼ同等の特性を示すことがわかる。
From the above, it can be seen that the catalyst using the metal catalyst carrier of the present example exhibits almost the same characteristics as the catalyst using the metal catalyst carrier of the comparative example.

【0018】[0018]

【発明の効果】本発明によると、市販されているコルゲ
ート状ハニカム体を用いた場合と同等の特性を示す金属
製の触媒担体を、容易に製造することができる。これに
より、熱伝導性、耐熱衝撃性、機械的強度等に優れる金
属製触媒担体を安価で提供することが可能となる。
According to the present invention, it is possible to easily produce a metal catalyst carrier having the same characteristics as those obtained when a commercially available corrugated honeycomb body is used. This makes it possible to provide a metal catalyst carrier excellent in thermal conductivity, thermal shock resistance, mechanical strength, and the like at low cost.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の実施例1の触媒担体に用いた金属箔体
の斜視図である。
FIG. 1 is a perspective view of a metal foil used for a catalyst carrier according to Example 1 of the present invention.

【図2】同実施例の触媒担体の中心軸に対する垂直断面
図である。
FIG. 2 is a vertical cross-sectional view of the catalyst carrier of the embodiment, taken along a central axis.

【図3】本発明の実施例2の触媒担体に用いた金属箔体
の斜視図である。
FIG. 3 is a perspective view of a metal foil used for a catalyst carrier according to Example 2 of the present invention.

【図4】同実施例3の触媒担体に用いた金属箔体の縦断
面図である。
FIG. 4 is a longitudinal sectional view of a metal foil used for a catalyst carrier of Example 3;

【図5】同実施例4の触媒担体の中心軸に対する垂直断
面図である。
FIG. 5 is a vertical sectional view with respect to a center axis of a catalyst carrier of Example 4.

【符号の説明】[Explanation of symbols]

1 金属箔体 2 平坦部 3 凸部 11 金属箔体 13 山 21 金属箔体 23 凸部 26 裂孔 31 金属箔体 35 金属棒 36 金属円筒 DESCRIPTION OF SYMBOLS 1 Metal foil body 2 Flat part 3 Convex part 11 Metal foil body 13 Mountain 21 Metal foil body 23 Convex part 26 Rupture 31 Metal foil body 35 Metal rod 36 Metal cylinder

───────────────────────────────────────────────────── フロントページの続き (72)発明者 川崎 良隆 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (72)発明者 保坂 正人 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 ──────────────────────────────────────────────────の Continued on the front page (72) Inventor Yoshitaka Kawasaki 1006 Kadoma Kadoma, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (72) Inventor Masato Hosaka 1006 Odaka Kadoma Kadoma City Osaka Pref.

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 表面に複数個の凸部を備えた金属箔体
を、前記金属箔体の平坦部が相互に密着しないように捲
回した円柱状の捲回体を具備する触媒担体。
1. A catalyst carrier comprising a columnar wound body formed by winding a metal foil body having a plurality of projections on its surface such that flat portions of the metal foil body do not adhere to each other.
【請求項2】 前記捲回体の外周側面に内接して配され
た筒状の金属部材を具備する請求項1記載の触媒担体。
2. The catalyst carrier according to claim 1, further comprising a cylindrical metal member inscribed on an outer peripheral side surface of the wound body.
【請求項3】 前記凸部が部分的に裂孔を有する請求項
1記載の触媒担体。
3. The catalyst carrier according to claim 1, wherein the projection has a partially broken hole.
【請求項4】 前記金属箔体が、Alを含むステンレス
鋼からなる請求項1記載の触媒担体。
4. The catalyst carrier according to claim 1, wherein said metal foil body is made of stainless steel containing Al.
【請求項5】 表面に複数個の凸部を備えた金属箔体の
端部を、棒状または筒状の芯材に接着したのち、前記芯
材を中心軸として、前記金属箔体を平坦部が相互に密着
しないように円柱状に捲回する触媒担体の製造法。
5. An end portion of a metal foil body having a plurality of convex portions on its surface is bonded to a rod-shaped or cylindrical core material, and the metal foil body is flattened with the core material as a central axis. A method for producing a catalyst carrier, wherein the catalyst carriers are wound in a columnar shape so that they do not adhere to each other.
JP8158481A 1996-06-19 1996-06-19 Catalyst carrier and method for producing the same Pending JPH10365A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8158481A JPH10365A (en) 1996-06-19 1996-06-19 Catalyst carrier and method for producing the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8158481A JPH10365A (en) 1996-06-19 1996-06-19 Catalyst carrier and method for producing the same

Publications (1)

Publication Number Publication Date
JPH10365A true JPH10365A (en) 1998-01-06

Family

ID=15672690

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8158481A Pending JPH10365A (en) 1996-06-19 1996-06-19 Catalyst carrier and method for producing the same

Country Status (1)

Country Link
JP (1) JPH10365A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100551525C (en) 2006-02-18 2009-10-21 三星Sdi株式会社 Hydrocarbon reforming catalyst, method of making same, and fuel processor containing same
DE102012020977A1 (en) * 2012-10-25 2014-05-15 Stanislav Volchkov Metal carrier, useful for producing waste gas catalyst, comprises a metal film having Archimedean spiral contour, and powder particles that are regularly arranged between coil windings and are welded to one broad side of the film
DE102006056483B4 (en) * 2006-11-30 2017-03-09 Vladimir Volchkov metal support
US20170183228A1 (en) * 2015-12-28 2017-06-29 Jiefeng Lin High aspect ratio catalytic reactor and catalyst inserts therefor

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN100551525C (en) 2006-02-18 2009-10-21 三星Sdi株式会社 Hydrocarbon reforming catalyst, method of making same, and fuel processor containing same
US7833934B2 (en) 2006-02-18 2010-11-16 Samsung Sdi Co., Ltd. Hydrocarbon reforming catalyst, method of preparing the same and fuel processor including the same
DE102006056483B4 (en) * 2006-11-30 2017-03-09 Vladimir Volchkov metal support
DE102012020977A1 (en) * 2012-10-25 2014-05-15 Stanislav Volchkov Metal carrier, useful for producing waste gas catalyst, comprises a metal film having Archimedean spiral contour, and powder particles that are regularly arranged between coil windings and are welded to one broad side of the film
US20170183228A1 (en) * 2015-12-28 2017-06-29 Jiefeng Lin High aspect ratio catalytic reactor and catalyst inserts therefor
US9938146B2 (en) * 2015-12-28 2018-04-10 Praxair Technology, Inc. High aspect ratio catalytic reactor and catalyst inserts therefor

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