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JPS6319220B2 - - Google Patents
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JPS6319220B2 - - Google Patents

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Publication number
JPS6319220B2
JPS6319220B2 JP56101324A JP10132481A JPS6319220B2 JP S6319220 B2 JPS6319220 B2 JP S6319220B2 JP 56101324 A JP56101324 A JP 56101324A JP 10132481 A JP10132481 A JP 10132481A JP S6319220 B2 JPS6319220 B2 JP S6319220B2
Authority
JP
Japan
Prior art keywords
catalyst
carrier
whiskers
microns
diameter
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
Application number
JP56101324A
Other languages
Japanese (ja)
Other versions
JPS583643A (en
Inventor
Sotoharu Goto
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP56101324A priority Critical patent/JPS583643A/en
Publication of JPS583643A publication Critical patent/JPS583643A/en
Publication of JPS6319220B2 publication Critical patent/JPS6319220B2/ja
Granted legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)

Description

【発明の詳細な説明】 本発明は、ウイスカからなる触媒担体に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a catalyst carrier consisting of whiskers.

従来触媒の担体として、直径3000ミクロン以上
の粒状ペレツトや、厚さ200ミクロン以上のハニ
カム形状の耐火物が使用されているが、これらは
担体の表面積に対する熱容量が大きく(ガスと接
触しない部分が多い。)、始動性に欠ける等の欠点
がある。そこで、本発明者らは、さきに、ガラス
繊維は直径が6〜9ミクロンで、ガスとの接触面
積が大きく、熱容量が小さいので、始動性に優れ
ている長所を見い出し、触媒担体として、90%以
上のシリカ分を含有する耐熱ガラス繊維を使用す
る触媒を発表し(特公昭53−38264号):更に、こ
のガラス繊維の表面に均一な触媒フイルム層を形
成させる方法を発表した(特公昭51−21629号)。
Conventionally, granular pellets with a diameter of 3,000 microns or more and honeycomb-shaped refractories with a thickness of 200 microns or more have been used as carriers for catalysts, but these have a large heat capacity relative to the surface area of the carrier (there are many parts that do not come into contact with gas). ), it has drawbacks such as poor startability. Therefore, the present inventors first discovered that glass fiber has a diameter of 6 to 9 microns, has a large contact area with gas, and has a small heat capacity, so it has excellent starting properties. announced a catalyst using heat-resistant glass fibers containing more than 10% silica (Japanese Patent Publication No. 38264/1989); and also announced a method for forming a uniform catalyst film layer on the surface of this glass fiber (Japanese Patent Publication No. 38264/1989). 51-21629).

ところで、担体として使用するガラス繊維の1
本のフイラメント(単繊維)の直径が小さくなれ
ばなる程、単位重量当りの表面積が増加し、一方
ガスとの接触面積に対する熱容量が減少する。こ
の事実を極限に近づければ、触媒表面の活性化エ
ネルギーが担体にうばわれることなく、ガス体に
伝達されるため、触媒の始動温度が低下すること
となる。この関係、即ち、担体の厚さ(ミクロ
ン)に対する始動温度(℃)の影響を第1図に示
す。
By the way, one of the glass fibers used as a carrier
The smaller the diameter of the book filament, the more the surface area per unit weight, while the heat capacity relative to the area in contact with the gas decreases. If this fact is approached to the limit, the activation energy on the surface of the catalyst will be transferred to the gas body without being carried away by the carrier, which will lower the starting temperature of the catalyst. This relationship, ie the effect of starting temperature (° C.) on carrier thickness (microns), is shown in FIG.

本発明者らは、上記事実に着目し、その極限に
近づくことを意図して、針状結晶の内、特に微細
な毛状単結晶繊維、即ち、ウイスカを触媒担体と
して使用することを試みた。
The present inventors focused on the above fact, and attempted to use particularly fine hair-like single crystal fibers, i.e., whiskers, as a catalyst carrier among needle-like crystals, with the intention of approaching the limit. .

今日、ウイスカの製造は金属に限らず、耐火物
においても盛んに製造されるようになり、例えば
アルミナ系、シリカ系、チタニア系等がそれであ
り、特にチタニア系では、チタニア水和物、チタ
ン酸バリウム、チタン酸カリウム等が知られてい
る。これらのウイスカを使用して触媒を製造しよ
うと試みることは、今日始まつたことではないけ
れども、現実にウイスカを使用して触媒を製造
し、具体的に前述した触媒性能、特に始動温度が
著しく低下したものが、今日まで現出していな
い。これは、今日まで微細な毛状の単結晶繊維で
あるウイスカの表面に、触媒成分を均一にコーテ
ングする手段が確立していなかつた点に起因して
いる。即ち、従来の触媒成分の担体へのコーテン
グ手段では、ウイスカの表面に、触媒成分を、均
一に、かつ、極めて薄いフイルム状に形成させる
ことが不可能であるとされている。これは、触媒
成分含有溶液が蒸発又は濃縮する際に、担体の表
面から移動したり又はその表面に凝集が生じた
り、更には、担体表面でブリツジ(架橋)現象が
生じたりするからであるとされている。
Today, the production of whiskers is not limited to metals, but is also actively produced in refractories, such as alumina-based, silica-based, titania-based, etc. Among the titania-based whiskers, especially titania hydrate, titanic acid, etc. Barium, potassium titanate, etc. are known. Attempts to manufacture catalysts using these whiskers are not new today, but in reality, catalysts have been manufactured using whiskers, and the performance of the catalysts mentioned above, especially the start-up temperature, has been significantly improved. What has deteriorated has not appeared to this day. This is due to the fact that until now, no means has been established for uniformly coating the surface of whiskers, which are fine hair-like single crystal fibers, with catalyst components. That is, it is said that it is impossible to uniformly form the catalyst component on the surface of the whisker in the form of an extremely thin film using conventional means for coating the carrier with the catalyst component. This is because when the catalyst component-containing solution evaporates or concentrates, it moves from the surface of the carrier or aggregates on the surface, and furthermore, a bridging phenomenon occurs on the surface of the carrier. has been done.

本発明者らは、これら液体の物性領域、即ち、
表面張力と毛管現象によつて生ずる上記欠点を、
触媒溶液にエステル化反応を導入して、ゲル化物
性を活用することによつて、上記欠点を解消する
ことができることを見い出した。本発明者らのこ
の手段は、基本的には、本発明者らが、さきに発
表した触媒成分の担体へのコーテング手段を用い
ているものである。この手段の概要は、触媒成分
となるべき金属の酸とアルコールとのエステルを
担体に被覆せしめ、このエステルを加熱下にゲル
化しつつ担体面に付着させ、次いでこれを焼成す
る方法である(特公昭51−21629号公報参照)。
The present inventors investigated the physical properties of these liquids, namely:
The above defects caused by surface tension and capillarity can be overcome by
It has been found that the above drawbacks can be overcome by introducing an esterification reaction into the catalyst solution and utilizing the gelling properties. This method of the present inventors basically uses the method of coating a catalyst component on a carrier, which the present inventors have previously announced. The outline of this method is to coat a carrier with an ester of a metal acid and an alcohol that is to be a catalyst component, apply the ester to the carrier surface while gelling it under heat, and then sinter it (specially (See Publication No. 51-21629).

本発明者らは、ウイスカ担体表面に、触媒成分
を均一に被覆させる方法として、上記ゲル化物性
を活用した方法を更に改良を加えたものである。
即ち、担体表面に、0.4ミクロン程度の厚さの触
媒層を形成する上記技術に改良を加え、その1/20
である0.02ミクロン厚さの触媒層を、ウイスカ担
体表面に形成する技術を確立したものである。
The present inventors have further improved the method utilizing the above-mentioned gelling property as a method for uniformly coating the surface of a whisker carrier with a catalyst component.
In other words, the above technology of forming a catalyst layer with a thickness of about 0.4 microns on the surface of the carrier has been improved, and the thickness is 1/20.
The technology has been established to form a catalyst layer with a thickness of 0.02 microns on the surface of a whisker carrier.

本発明は、この技術の確立によつて、今日まで
不可能視されていたウイスカからなる触媒担体を
完成したものである。即ち、本発明は、直径0.3
ミクロン以下の単結晶繊維(ウイスカ)をガラス
繊維又は金属線の表面に接着してなることを特徴
とする排ガス処理用触媒担体を要旨とするもので
ある。
With the establishment of this technology, the present invention has completed a catalyst carrier made of whiskers, which had been considered impossible until now. That is, the present invention has a diameter of 0.3
The gist of the present invention is a catalyst carrier for exhaust gas treatment, characterized in that it is formed by adhering submicron single crystal fibers (whiskers) to the surface of glass fibers or metal wires.

本発明に適用できるウイスカは、制限されるも
のではなく、金属系を含むすべてのウイスカを包
含するものであるが、どんな種類のウイスカを用
いたとしても、ウイスカ自体が直径0.3ミクロン
以下という極めて微細な単結晶繊維であるため、
これを、このままの形で触媒として使用できる適
用範囲は極めてせまいものである。
Whiskers that can be applied to the present invention are not limited and include all types of whiskers, including metal whiskers, but no matter what kind of whiskers are used, the whiskers themselves are extremely fine with a diameter of 0.3 microns or less. Because it is a single crystal fiber,
The range of applications in which it can be used as a catalyst in its current form is extremely narrow.

そこで本発明では、ウイスカをガラス繊維又は
金属線の表面に接着させて触媒担体とするのであ
る。
Therefore, in the present invention, whiskers are adhered to the surface of glass fiber or metal wire to form a catalyst carrier.

本発明では、ウイスカを接着させたガラス繊維
又は金属線を、綿状、フエルト状、糸状、布状又
は織物状に成形する。
In the present invention, glass fiber or metal wire to which whiskers are bonded is formed into a cotton-like, felt-like, thread-like, cloth-like, or woven-like form.

このようにして、本発明ではウイスカを適用範
囲の広い、実用的な触媒担体とするものである。
In this way, the present invention uses whiskers as a practical catalyst carrier with a wide range of applications.

この担体上に触媒成分を均一に被覆するに当つ
ては、予めウイスカをガラス繊維又は金属線の表
面に接着させた後にフイルム状の触媒層を形成さ
せるか、或いは接着後上記のように形成してから
フイルム状の触媒層を形成させるか、いづれの手
段をも本発明において採用できるものである。
In order to uniformly coat the catalyst component on this carrier, a film-like catalyst layer is formed after adhering the whiskers to the surface of the glass fiber or metal wire in advance, or alternatively, after adhesion, the catalyst component is formed as described above. Either method can be adopted in the present invention, such as forming a film-like catalyst layer after that.

本発明において、担体の表面に、触媒成分を均
一なフイルム状に形成させる方法としては、前述
したように、触媒成分含有溶液にエステル化反応
を導入して、ゲル化物性を活用する手段を採用す
るものであるが、この手段を、参考例および実施
例によつて具体的に詳細に説明する。
In the present invention, as a method for forming the catalyst component into a uniform film shape on the surface of the carrier, as described above, a method is adopted in which an esterification reaction is introduced into the catalyst component-containing solution and the gelling property is utilized. However, this means will be specifically explained in detail using reference examples and examples.

参考例 1 20モル%のクロム酸を含有する水溶液50部(重
量比、以下同じ)に、10モル%の酢酸マグネシウ
ム水溶液10部を加え、この混合溶液にプロピレン
グリコール20部を加えて1時間エステル化反応を
行わしめ、比較的安定化したエステル中間体80部
に、メタノール100部、水200部及び0.1モル%の
塩化パラジウム水溶液20部を加えて12時間放置す
る。この溶液400部を、チタン酸カリウムウイス
カ(直径0.1〜0.3ミクロン)200部に浸漬塗布し、
これを200℃で2時間加熱してエステル化反応を
完結させる。次いで、600℃で1時間焼成してエ
ステル分解を完了させて、ウイスカ表面に貴金属
を含む触媒金属の均一なフイルムを形成させ、更
に、水素を含む還元ガス雰囲気中で600℃1時間
活性化処理を行つた。このようにして製造した触
媒は0.1〜0.3ミクロン直径のウイスカ表面に、
0.02ミクロン厚さの均一な触媒フイルム層が形成
されているものである。
Reference Example 1 Add 10 parts of a 10 mol% magnesium acetate aqueous solution to 50 parts of an aqueous solution (weight ratio, same below) containing 20 mol% chromic acid, add 20 parts of propylene glycol to this mixed solution, and incubate for 1 hour. 100 parts of methanol, 200 parts of water, and 20 parts of a 0.1 mol % palladium chloride aqueous solution are added to 80 parts of the ester intermediate which has undergone the reaction and has become relatively stable, and is left to stand for 12 hours. 400 parts of this solution was applied by dip coating to 200 parts of potassium titanate whiskers (0.1 to 0.3 microns in diameter).
This is heated at 200°C for 2 hours to complete the esterification reaction. Next, ester decomposition is completed by baking at 600°C for 1 hour to form a uniform film of catalytic metal containing precious metals on the whisker surface, followed by activation treatment at 600°C for 1 hour in a reducing gas atmosphere containing hydrogen. I went to The catalyst produced in this way has a whisker surface with a diameter of 0.1 to 0.3 microns.
A uniform catalyst film layer with a thickness of 0.02 microns is formed.

第2図のCは、このように製造した触媒の断面
図である。なお、第2図中のA及びBは、参考と
してあげたものであつて、Aは、直径6ミクロン
のガラス繊維担体の表面に、0.4ミクロン厚さの
均一な触媒フイルム層を形成させたものであり、
Bは、直径1ミクロンのセラミツクス短繊維担体
の表面に、0.1ミクロン厚さの均一な触媒フイル
ム層を形成させたものであり、これらA、B触媒
はいづれも触媒成分含有溶液にエステル化反応を
導入して、ゲル化物性を活用する手段を採用して
製造したものである。
FIG. 2C is a cross-sectional view of the catalyst thus produced. Note that A and B in Figure 2 are for reference only, and A is a case in which a uniform catalyst film layer of 0.4 microns in thickness is formed on the surface of a glass fiber carrier with a diameter of 6 microns. and
Catalyst B has a uniform catalyst film layer of 0.1 micron thickness formed on the surface of a ceramic short fiber carrier with a diameter of 1 micron. Both catalysts A and B carry out an esterification reaction in a catalyst component-containing solution. This product was manufactured using a method that utilizes gelling properties.

参考例 2 直径0.1〜0.3ミクロン直径のチタン酸カリウム
ウイスカ担体を使用し、このウイスカ自体を焼成
して、直径3〜4mmのペレツトに成形し、このウ
イスカペレツトの表面に、参考例1と同様の方法
で、均一なフイルム状触媒層を形成させた。
Reference Example 2 A potassium titanate whisker carrier with a diameter of 0.1 to 0.3 microns was used, the whiskers themselves were fired and formed into pellets with a diameter of 3 to 4 mm, and the surface of the whisker pellets was coated with the same method as in Reference Example 1. In this way, a uniform film-like catalyst layer was formed.

この触媒を、両端開口、金網張りの円筒に入
れ、これを自動車公害防止対策(駐車場の排ガス
処理)に適用したところ、一酸化炭素濃度
1200ppmを含む空気を、SV値(空間速度)10000
毎時で通過せしめ、処理ガス温度25℃の条件下
で、91.4%の浄化率を得た。
When this catalyst was placed in a cylinder with openings at both ends and lined with wire mesh, and applied to automobile pollution prevention measures (exhaust gas treatment in parking lots), the carbon monoxide concentration was
Air containing 1200ppm, SV value (space velocity) 10000
A purification rate of 91.4% was obtained under conditions where the gas was passed every hour and the processing gas temperature was 25°C.

実施例 酸化チタンウイスカ(TiO298.5%、繊維径0.1
〜0.3ミクロン)の粉末を、アルミナゾル水溶液
に混合し、これを9ミクロン直径のフイラメント
から形成されたガラス繊維布(14メツシユ相当網
目)の表面に浸漬塗布し、150℃で2時間、600℃
で1時間の熱処理後、参考例1と同様、白金主体
の均一な触媒フイルムを形成した。
Example Titanium oxide whisker (TiO 2 98.5%, fiber diameter 0.1
~0.3 micron) powder was mixed with an alumina sol aqueous solution, and this was applied by dip coating onto the surface of a glass fiber cloth (mesh equivalent to 14 mesh) formed from a filament with a diameter of 9 microns, and heated at 150°C for 2 hours and at 600°C.
After heat treatment for 1 hour, a uniform catalyst film mainly composed of platinum was formed as in Reference Example 1.

この触媒布10枚を重ね、塗装乾燥炉の排ガス処
理に使用し、入口ガス温度82℃、炭化水素含有量
1150ppm、残部空気の排ガスを空間速度毎時
10000の条件で通過させ、炭化水素94.7%の除去
率を得た。
10 sheets of this catalyst cloth were stacked and used to treat the exhaust gas of a paint drying oven, and the inlet gas temperature was 82℃ and the hydrocarbon content was
1150ppm, residual air exhaust gas space velocity per hour
It was passed under the conditions of 10000, and a hydrocarbon removal rate of 94.7% was obtained.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、担体の厚さ(ミクロン)に対する始
動温度(℃)の関係を示す。第2図は、3種類の
繊維担体からなる触媒の断面図である。
FIG. 1 shows the relationship between starting temperature (° C.) and support thickness (in microns). FIG. 2 is a cross-sectional view of a catalyst composed of three types of fiber carriers.

Claims (1)

【特許請求の範囲】[Claims] 1 直径0.3ミクロン以下の単結晶繊維(ウイス
カ)をガラス繊維又は金属線の表面に接着してな
ることを特徴とする排ガス処理用触媒担体。
1. A catalyst carrier for exhaust gas treatment, characterized in that it is made by bonding single crystal fibers (whiskers) with a diameter of 0.3 microns or less to the surface of glass fibers or metal wires.
JP56101324A 1981-07-01 1981-07-01 Catalyst using whisker as carrier Granted JPS583643A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56101324A JPS583643A (en) 1981-07-01 1981-07-01 Catalyst using whisker as carrier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56101324A JPS583643A (en) 1981-07-01 1981-07-01 Catalyst using whisker as carrier

Publications (2)

Publication Number Publication Date
JPS583643A JPS583643A (en) 1983-01-10
JPS6319220B2 true JPS6319220B2 (en) 1988-04-21

Family

ID=14297633

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56101324A Granted JPS583643A (en) 1981-07-01 1981-07-01 Catalyst using whisker as carrier

Country Status (1)

Country Link
JP (1) JPS583643A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0279428U (en) * 1988-12-06 1990-06-19

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61212335A (en) * 1985-03-18 1986-09-20 Hitachi Zosen Corp Glass fiber catalyst holding catalytic component and its preparation
JP4639536B2 (en) * 2001-06-15 2011-02-23 スズキ株式会社 Exhaust gas purification catalyst and method for producing the same

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0279428U (en) * 1988-12-06 1990-06-19

Also Published As

Publication number Publication date
JPS583643A (en) 1983-01-10

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