JPH04313347A - Production of catalyst supporting metal or metal oxide - Google Patents

Production of catalyst supporting metal or metal oxide

Info

Publication number
JPH04313347A
JPH04313347A JP3106861A JP10686191A JPH04313347A JP H04313347 A JPH04313347 A JP H04313347A JP 3106861 A JP3106861 A JP 3106861A JP 10686191 A JP10686191 A JP 10686191A JP H04313347 A JPH04313347 A JP H04313347A
Authority
JP
Japan
Prior art keywords
metal
catalyst
metal oxide
water
supported
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
JP3106861A
Other languages
Japanese (ja)
Inventor
Chihiro Nakanishi
中西 千博
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.)
Tanaka Kikinzoku Kogyo KK
Original Assignee
Tanaka Kikinzoku Kogyo KK
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 Tanaka Kikinzoku Kogyo KK filed Critical Tanaka Kikinzoku Kogyo KK
Priority to JP3106861A priority Critical patent/JPH04313347A/en
Publication of JPH04313347A publication Critical patent/JPH04313347A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To provide the method of producing a highly active catalyst compris ing a water-repellent carrier such as org. polymers on which metal or metal oxide is suspported. CONSTITUTION:The above catalyst carrying metal or metal oxide can be obtd. by supporting an org. metal compd. on a water-repellent carrier and then converting the supported org. metal compd. into metal or metal oxide corresponding the org. metal compd.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は、有機ポリマー等の撥水
性担体に金属や金属酸化物を担持させて各種用途に使用
できる触媒を製造するための方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a catalyst that can be used for various purposes by supporting a metal or metal oxide on a water-repellent carrier such as an organic polymer.

【0002】0002

【従来技術とその問題点】撥水性担体に触媒粒子を担持
させて成る触媒は有機合成反応等において特異な性質を
有している。例えばガスクロマトグラム用カラム充填剤
として多用されているポラパック(Porapak)Q
(商品名、スチレン−ジビニルベンゼン共重合体)に白
金を担持させた触媒はD2−H2OのD−H交換反応に
おいて低温で特異な活性を示すことが報告されている。 この撥水性物質を担体とする触媒を製造する際に、例え
ば塩化白金酸のアセトン溶液にポラパックQを浸漬し溶
媒を除去した後、水素還元を行って触媒を製造すること
が試みられているが、塩化白金酸等の無機塩は親油性に
乏しいためポラパックQに対する親和性が弱く、溶媒を
留去する際に微結晶として担体表面上に析出する。そし
て析出した塩化白金酸の結晶を水素還元しているため、
担持金属の分散度が低く高活性な触媒を得ることができ
ないという欠点がある。
[Prior Art and its Problems] A catalyst comprising catalyst particles supported on a water-repellent carrier has unique properties in organic synthesis reactions and the like. For example, Porapak Q is widely used as a column packing material for gas chromatography.
It has been reported that a catalyst in which platinum is supported on (trade name, styrene-divinylbenzene copolymer) exhibits unique activity at low temperatures in the D-H exchange reaction of D2-H2O. When producing a catalyst using this water-repellent material as a carrier, attempts have been made to, for example, immerse Polapack Q in an acetone solution of chloroplatinic acid, remove the solvent, and then perform hydrogen reduction to produce the catalyst. Inorganic salts such as chloroplatinic acid and the like have poor lipophilicity and therefore have a weak affinity for Polapac Q, and when the solvent is distilled off, they precipitate on the surface of the carrier as microcrystals. Since the precipitated chloroplatinic acid crystals are then reduced with hydrogen,
There is a drawback that the degree of dispersion of the supported metal is low and a highly active catalyst cannot be obtained.

【0003】0003

【発明の目的】本発明は、上述の撥水性担体により生ず
る特異な触媒特性を有効利用するために、前記撥水性担
体に金属や金属酸化物を高度に分散させて高活性の触媒
を製造する方法を提供することを目的とする。
[Object of the Invention] In order to effectively utilize the unique catalytic properties produced by the above-mentioned water-repellent carrier, the present invention involves producing a highly active catalyst by highly dispersing metals and metal oxides in the water-repellent carrier. The purpose is to provide a method.

【0004】0004

【問題点を解決するための手段】本発明は、撥水性担体
に有機金属化合物を担持し、担持した前記有機金属化合
物を対応する金属又は金属酸化物に変換することを特徴
とする金属又は金属酸化物担持触媒の製造方法である。
[Means for Solving the Problems] The present invention provides a metal or metal compound characterized in that an organometallic compound is supported on a water-repellent carrier and the supported organometallic compound is converted into a corresponding metal or metal oxide. This is a method for producing an oxide-supported catalyst.

【0005】以下本発明を詳細に説明する。本発明に係
わる触媒製造方法では、撥水性担体つまり親油性の担体
に親油性のない金属や金属酸化物を担持させる際に、該
金属等と同様に親油性に乏しい無機化合物を使用する代
わりに、親油性に富む有機金属化合物を使用して高分散
度の金属や金属酸化物を前記撥水性担体に担持させるこ
とを意図するものである。
The present invention will be explained in detail below. In the catalyst production method according to the present invention, when supporting a non-lipophilic metal or metal oxide on a water-repellent carrier, that is, a lipophilic carrier, instead of using an inorganic compound that has poor lipophilicity like the metal, etc. , it is intended that a highly dispersed metal or metal oxide be supported on the water-repellent carrier by using an organometallic compound that is highly lipophilic.

【0006】従って使用する有機金属化合物は、担持す
べき触媒金属を含有すればよく、その他は特に限定され
ないが、該化合物中にハロゲン原子や窒素原子を含有す
るとこれらの原子から形成されるガスや化合物例えばハ
ロゲンガスや窒素酸化物、アンモニア等が担体上に触媒
毒として残留し易く又触媒製造時に有害ガスを発生し易
くなるため、これらの原子等を含有しないか含有量が僅
少である有機化合物であることが望ましい。このような
化合物としては、例えば有機酸の金属塩やアセチルアセ
トン化合物、π−アリル化合物等があるが、コスト及び
入手し易さから有機酸の金属塩を使用することが望まし
い。前記有機酸としは、オクチル酸、デカン酸、ネオデ
カン酸、ステアリン酸等があり、該有機酸は炭素数が2
以上で炭素、水素及び酸素のみから成ることが望ましい
。しかし例えば水素1個が塩素置換されたモノ置換ステ
アリン酸のような場合には全体に対する塩素含有量が僅
少であり、塩化白金酸の場合のような高塩素含有量では
ないため、仮に有害ガス発生や触媒毒発生が生じてもさ
ほど触媒活性に影響を与えることがなく、本発明方法に
おいて使用することができる。又上述した1価の有機酸
だけでなくグルタル酸等の多価有機酸を使用してもよい
[0006] Therefore, the organometallic compound used is not particularly limited as long as it contains the catalyst metal to be supported, but if the compound contains a halogen atom or a nitrogen atom, gas or Compounds such as halogen gas, nitrogen oxides, ammonia, etc. tend to remain as catalyst poisons on the carrier and generate harmful gases during catalyst production, so organic compounds that do not contain these atoms or contain only a small amount of these atoms, etc. It is desirable that Such compounds include, for example, metal salts of organic acids, acetylacetone compounds, π-allyl compounds, etc., but it is desirable to use metal salts of organic acids because of cost and availability. Examples of the organic acid include octylic acid, decanoic acid, neodecanoic acid, stearic acid, etc., and the organic acid has 2 carbon atoms.
In the above, it is preferable that the material consists of only carbon, hydrogen, and oxygen. However, for example, in the case of mono-substituted stearic acid in which one hydrogen is replaced with chlorine, the chlorine content in the whole is very small, and it is not as high as the chlorine content in the case of chloroplatinic acid. Even if catalyst poisoning occurs, the catalyst activity is not significantly affected and can be used in the method of the present invention. In addition to the above-mentioned monovalent organic acids, polyvalent organic acids such as glutaric acid may also be used.

【0007】又金属としては、白金、パラジウム、イリ
ジウム、ロジウム、ルテニウム、金、銀等の貴金属の他
に、鉄、ニッケル、コバルト等の卑金属があり、所望の
触媒活性がある限り特に限定されない。
Metals include noble metals such as platinum, palladium, iridium, rhodium, ruthenium, gold, and silver, as well as base metals such as iron, nickel, and cobalt, and are not particularly limited as long as they have the desired catalytic activity.

【0008】使用する撥水性担体は、必要とする触媒特
性に応じて選択すれば良く、一般に該撥水性担体として
は有機ポリマーをビーズ状に成型したものが使用される
[0008] The water-repellent carrier to be used may be selected depending on the required catalytic properties, and generally, organic polymers molded into beads are used as the water-repellent carrier.

【0009】本発明では、上記した有機金属化合物をア
ルコール類、ケトン類、エーテル類等の有機溶媒に溶解
した溶液に、前述のポラパックQ等の撥水性担体を浸漬
し、含浸した該有機金属化合物に熱分解等を施して対応
する金属酸化物に変換して金属酸化物担持触媒を製造し
(白金の場合には白金担持触媒)、金属担持触媒が必要
な場合には必要に応じて水素還元して所定の触媒を製造
する。熱分解自体は従来の熱分解条件に従って行えばよ
い。又前記溶媒としてあまり粘度の高いものを使用する
と担体を浸漬する際に前記有機金属化合物が浸入し難く
なるため好ましくない。又該溶媒がハロゲンや窒素を含
有すると溶媒から有害ガスが発生したり触媒毒が生じた
りするため使用する溶媒は上述した窒素やハロゲンを含
まない溶媒とすることが好ましい。
In the present invention, a water-repellent carrier such as the above-mentioned Polapack Q is immersed in a solution of the above-mentioned organometallic compound dissolved in an organic solvent such as an alcohol, a ketone, or an ether, and the organometallic compound is impregnated with the water-repellent carrier. is converted into the corresponding metal oxide by thermal decomposition etc. to produce a metal oxide supported catalyst (in the case of platinum, a platinum supported catalyst), and if a metal supported catalyst is required, hydrogen reduction is performed as necessary. A predetermined catalyst is produced. Thermal decomposition itself may be carried out according to conventional thermal decomposition conditions. Furthermore, it is not preferable to use a solvent with too high a viscosity because it becomes difficult for the organometallic compound to penetrate when the carrier is immersed. Further, if the solvent contains halogen or nitrogen, harmful gases or catalyst poisons may be generated from the solvent, so it is preferable that the solvent used does not contain the above-mentioned nitrogen or halogen.

【0010】このように本発明方法では親水性の触媒金
属を担持し難い撥水性担体にこれらの触媒金属あるいは
金属酸化物を担持する際に、該金属を含有する有機金属
化合物を前記撥水性担体に高分散状態で担持させた後、
熱分解法等の適宜の手段で対応する金属又は金属酸化物
に変換するようにしている。従って本発明方法によると
触媒担体として特異な性質を有する撥水性担体に高分散
状態で触媒金属又は金属酸化物を担持させることができ
、活性が高くユニークな触媒特性を有する触媒を製造す
ることが可能になる。
As described above, in the method of the present invention, when supporting a hydrophilic catalyst metal or a metal oxide on a water-repellent carrier that is difficult to support, an organometallic compound containing the metal is transferred to the water-repellent carrier. After being supported in a highly dispersed state,
It is converted into the corresponding metal or metal oxide by appropriate means such as thermal decomposition. Therefore, according to the method of the present invention, it is possible to support a catalytic metal or metal oxide in a highly dispersed state on a water-repellent carrier having unique properties as a catalyst carrier, and it is possible to produce a catalyst with high activity and unique catalytic properties. It becomes possible.

【0011】次に本発明による触媒製造の実施例を記載
するが、本発明はこの実施例に限定されるものではない
Next, an example of the production of a catalyst according to the present invention will be described, but the present invention is not limited to this example.

【0012】0012

【実施例】オクチル酸白金塩のアセトン溶液にポラパッ
クQを浸漬し、真空乾燥によってアセトンを留去した後
、水素気流中250 ℃で3時間還元を行い、その後1
2時間真空乾燥して5%白金/ポラパックQ触媒を得た
。粉末X線回折法によって担持白金粒子の粒径を測定し
たところ30Å以下であり高分散していることが確認さ
れた。
[Example] Polapack Q was immersed in an acetone solution of octylic acid platinum salt, the acetone was distilled off by vacuum drying, and then reduction was performed at 250 °C for 3 hours in a hydrogen stream, and then 1
After vacuum drying for 2 hours, a 5% platinum/Porapack Q catalyst was obtained. When the particle size of the supported platinum particles was measured by powder X-ray diffraction, it was found to be 30 Å or less, indicating that the platinum particles were highly dispersed.

【0013】[0013]

【比較例】オクチル酸白金塩の代わりに塩化白金酸のア
セトン溶液を使用して実施例と同一条件で5%白金/ポ
ラパックQ触媒を得た。粉末X線回折法によって担持白
金粒子の粒径を測定したところ70Åであった。
[Comparative Example] A 5% platinum/Polapack Q catalyst was obtained under the same conditions as in the example except that an acetone solution of chloroplatinic acid was used instead of platinum octylate salt. The particle size of the supported platinum particles was measured by powder X-ray diffraction and was 70 Å.

【0014】[0014]

【発明の効果】本発明は、撥水性担体に有機金属化合物
を担持し、担持した前記有機金属化合物を対応する金属
又は金属酸化物に変換することを特徴とする金属又は金
属酸化物担持触媒の製造方法(請求項1)である。撥水
性担体を使用する金属触媒は特異な反応活性を示す反面
、無機化合物に対する親和性が乏しく、従来の無機化合
物を使用する熱分解法で製造しても高分散度の活性の高
い触媒を製造できないという欠点がある。しかし本発明
方法では、前記無機化合物の代わりに前記撥水性担体に
親和性のある有機金属化合物を使用して触媒金属を前記
担体上に高分散状態で担持させ、その後対応する金属又
は金属酸化物に変換するようにしているため、高活性で
特異な反応特性を触媒を製造することができる。そして
使用する有機金属化合物として前記金属及び炭素、水素
及び酸素のみから成る化合物を使用すると(請求項2)
、該化合物には有害ガスを発生させたり触媒毒を生じさ
せ易いハロゲンや窒素が含有されていないため、製造作
業中に該作業を阻害するほどの有害ガスを発生したり製
造される触媒の活性を大きく低下されるほどの触媒毒を
生じさせることがなく、より高活性な触媒を安全な操業
で製造することができる。前記有機金属化合物の対応す
る金属又は金属酸化物への変換は通常の熱分解法とする
ことが好ましく(請求項3)、該方法により効率良くか
つ容易に対応する金属等に変換することができる。 前記有機金属化合物としてはアセチルアセトンやπ−ア
リル化合物等の使用も可能であるが、低コストで入手が
容易な有機酸の金属塩(請求項4)とすることが望まし
い。
Effects of the Invention The present invention provides a catalyst supported on a metal or metal oxide, which is characterized in that an organic metal compound is supported on a water-repellent carrier, and the supported organic metal compound is converted into a corresponding metal or metal oxide. A manufacturing method (claim 1). Although metal catalysts that use water-repellent carriers exhibit unique reaction activity, they have poor affinity for inorganic compounds, and even if they are produced using conventional thermal decomposition methods that use inorganic compounds, highly active catalysts with high dispersion can be produced. The drawback is that it cannot be done. However, in the method of the present invention, an organometallic compound having an affinity for the water-repellent carrier is used instead of the inorganic compound, the catalyst metal is supported on the carrier in a highly dispersed state, and then the corresponding metal or metal oxide is This allows the production of catalysts with high activity and unique reaction characteristics. When a compound consisting only of the metal, carbon, hydrogen and oxygen is used as the organometallic compound (Claim 2)
Since the compound does not contain halogen or nitrogen, which tend to generate harmful gases or poison the catalyst, it may generate harmful gases during the production process that would impede the production process, or reduce the activity of the catalyst being produced. It is possible to produce a highly active catalyst in a safe manner without producing catalyst poisons that would significantly reduce the performance of the catalyst. The conversion of the organometallic compound into the corresponding metal or metal oxide is preferably carried out by a normal thermal decomposition method (claim 3), and by this method, it can be efficiently and easily converted into the corresponding metal, etc. . Although it is possible to use acetylacetone, a π-allyl compound, etc. as the organometallic compound, it is preferable to use a metal salt of an organic acid which is inexpensive and easily available (claim 4).

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】  撥水性担体に有機金属化合物を担持し
、担持した前記有機金属化合物を対応する金属又は金属
酸化物に変換することを特徴とする金属又は金属酸化物
担持触媒の製造方法。
1. A method for producing a metal or metal oxide-supported catalyst, which comprises supporting an organometallic compound on a water-repellent carrier and converting the supported organometallic compound into a corresponding metal or metal oxide.
【請求項2】  有機金属化合物が金属及び、炭素、水
素及び酸素のみから成る請求項1に記載の方法。
2. The method according to claim 1, wherein the organometallic compound consists only of metal, carbon, hydrogen and oxygen.
【請求項3】  有機金属化合物の変換を熱分解法によ
り行う請求項1又は2に記載の方法。
3. The method according to claim 1, wherein the organometallic compound is converted by a pyrolysis method.
【請求項4】  有機金属化合物が有機酸の金属塩であ
る請求項1から3までのいずれかに記載の方法。
4. The method according to claim 1, wherein the organometallic compound is a metal salt of an organic acid.
JP3106861A 1991-04-11 1991-04-11 Production of catalyst supporting metal or metal oxide Pending JPH04313347A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3106861A JPH04313347A (en) 1991-04-11 1991-04-11 Production of catalyst supporting metal or metal oxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3106861A JPH04313347A (en) 1991-04-11 1991-04-11 Production of catalyst supporting metal or metal oxide

Publications (1)

Publication Number Publication Date
JPH04313347A true JPH04313347A (en) 1992-11-05

Family

ID=14444354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3106861A Pending JPH04313347A (en) 1991-04-11 1991-04-11 Production of catalyst supporting metal or metal oxide

Country Status (1)

Country Link
JP (1) JPH04313347A (en)

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