JPH067921B2 - Method for producing supported catalyst - Google Patents
Method for producing supported catalystInfo
- Publication number
- JPH067921B2 JPH067921B2 JP60153297A JP15329785A JPH067921B2 JP H067921 B2 JPH067921 B2 JP H067921B2 JP 60153297 A JP60153297 A JP 60153297A JP 15329785 A JP15329785 A JP 15329785A JP H067921 B2 JPH067921 B2 JP H067921B2
- Authority
- JP
- Japan
- Prior art keywords
- carrier
- metal element
- white metal
- palladium
- 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.)
- Expired - Lifetime
Links
Description
【発明の詳細な説明】 (産業上の利用分野) 本発明は多孔性担体(以下「担体」と称す。)への白金
属元素の担持方法に関するものである。更に詳しくは、
白金属元素の全部または大部分を担体の表層部に担持さ
せた担持触媒の製造方法に関するものである。The present invention relates to a method for supporting a white metal element on a porous carrier (hereinafter referred to as "carrier"). For more details,
The present invention relates to a method for producing a supported catalyst in which all or most of the white metal element is supported on the surface layer of a carrier.
(従来の技術) 白金属元素を担体に担持した担持触媒は各種有機化合物
の水素化反応、水素化分解反応、自動車排ガスの接触転
化反応等に広く利用されるが、一般にこれらの反応は非
常に速いため触媒粒子の外部表面で進行し触媒粒内部の
金属は有効に使用されない。従って高価な白金属元素を
触媒物質として使用する場合には担体の表層部に白金属
元素を高密度に担持して効果的に使用する必要がある。(Prior Art) A supported catalyst in which a white metal element is supported on a carrier is widely used for hydrogenation reaction of various organic compounds, hydrocracking reaction, catalytic conversion reaction of automobile exhaust gas, etc. Because of its high speed, it advances on the outer surface of the catalyst particles and the metal inside the catalyst particles is not effectively used. Therefore, when an expensive white metal element is used as a catalyst substance, it is necessary to support the white metal element at a high density on the surface layer of the carrier for effective use.
従来白金属元素を担体の表層部に担持させる方法として
は、塩基性固体酸化物担体あるいは前処理して塩基性に
した担体に白金属元素化合物の水溶液を加えて担体表面
の塩基によって加水分解を起こさせ、白金属元素を表層
部に沈着させる方法が知られている。しかしながらこの
方法によると担体に制限があり、担体の種類によっては
白金属元素が担体内部にまで浸透しその目的を達し得な
い場合がある。Conventionally, as a method of supporting a white metal element on the surface layer of a carrier, a basic solid oxide carrier or a pretreated basic carrier is added with an aqueous solution of a white metal element compound and hydrolyzed by a base on the carrier surface. There is known a method of causing the white metal element to deposit on the surface layer portion. However, according to this method, the carrier is limited, and depending on the type of the carrier, the white metal element may permeate into the inside of the carrier and the purpose may not be achieved.
そのために白金属元素化合物の水溶液のpHを調整する方
法(特公昭47-35670号公報)、白金属元素化合物のアセ
トン溶液を含浸液として用いる方法(特開昭48-53980号
公報)、ポリエチレングリコールまたは非イオン系界面
活性剤を含浸液に添加する方法(特開昭49-111886号公
報、特開昭49-114588号公報)、クエン酸溶液を触媒担
体に予備含浸させる方法(特開昭54-149391号公報)等
が提案されている。しかしいずれの方法においても白金
属元素の担体の表層部のみでなく内部にも侵入する場合
があり、必ずしもその目的を達し得ない。また方法によ
っては触媒活性が低下することがある。For that purpose, a method of adjusting the pH of an aqueous solution of a white metal element compound (Japanese Patent Publication No. 47-35670), a method of using an acetone solution of a white metal element compound as an impregnating liquid (Japanese Patent Publication No. 48-53980), polyethylene glycol Alternatively, a method of adding a nonionic surfactant to the impregnating solution (JP-A-49-111886 and JP-A-49-114588), and a method of pre-impregnating a catalyst carrier with a citric acid solution (JP-A-54) -149391 gazette) etc. are proposed. However, in any of the methods, the white metal element may penetrate not only into the surface layer portion of the carrier but also into the inside thereof, and the purpose cannot always be achieved. In addition, the catalytic activity may decrease depending on the method.
(発明が解決しようとする問題点) 本発明が解決しようとする問題点、即ち本発明の目的は
上記のような従来法の欠点を取り除き、非常に簡単にし
かも安価に担体の表層部に白金属元素を担持せしめる方
法を提供するものである。すなわち担体をあらかじめ炭
素数5ないし12の炭化水素化合物に浸漬させた後、白
金属元素の水溶液を担体に含浸させることにより白金属
元素の全部または大部分が担体の表層部に担持されるこ
とを見い出したものである。(Problems to be Solved by the Invention) A problem to be solved by the present invention, that is, an object of the present invention is to eliminate the drawbacks of the conventional methods as described above, and to make the surface layer of the carrier white in a very simple and inexpensive manner. It is intended to provide a method for supporting a metal element. That is, by immersing the carrier in advance in a hydrocarbon compound having 5 to 12 carbon atoms and then impregnating the carrier with an aqueous solution of a white metal element, all or most of the white metal element is supported on the surface layer portion of the carrier. It has been found.
(問題点を解決する為の手段) 本発明において用いられる炭素数5ないし12の炭化水
素化合物としてはペンタン、ヘキサン、オクタン、ペン
テン、ヘキセン等の脂肪族炭化水素、シクロペンタン、
シクロヘキサン、メチルシクロペンタン等の脂環式炭化
水素、それにベンゼン、トルエン、キシレン、エチルベ
ンゼン等の芳香族炭化水素があり、好ましくは炭素数6
ないし10の炭化水素化合物が用いられる。これらの炭
化水素化合物は単独で用いてもよいし、二つ以上を混合
して用いてもよい。(Means for Solving Problems) Examples of the hydrocarbon compound having 5 to 12 carbon atoms used in the present invention include aliphatic hydrocarbons such as pentane, hexane, octane, pentene and hexene, cyclopentane,
There are alicyclic hydrocarbons such as cyclohexane and methylcyclopentane, and aromatic hydrocarbons such as benzene, toluene, xylene, and ethylbenzene, preferably having 6 carbon atoms.
To 10 hydrocarbon compounds are used. These hydrocarbon compounds may be used alone or in combination of two or more.
担体を炭化水素化合物中に浸漬させる条件については特
に限定されるものではないが、通常は室温条件下に担体
を10分間ないし10時間炭化水素化合物中に浸漬させ
る。The conditions for immersing the carrier in the hydrocarbon compound are not particularly limited, but usually the carrier is immersed in the hydrocarbon compound for 10 minutes to 10 hours at room temperature.
本発明方法において用いられる担体は表面積1〜1000m2
/gの多孔性担体である。具体的にはアルミナ、シリカ、
シリカアルミナ、マグネシア、チタニア、ジルコニア、
酸化ニオブ等がある。本発明方法において多孔性担体で
あれば特に制限はないが、酸性を有する担体において従
来法と比較して顕著にその効果が発揮される。The carrier used in the method of the present invention has a surface area of 1 to 1000 m 2.
/ g of porous carrier. Specifically, alumina, silica,
Silica-alumina, magnesia, titania, zirconia,
There are niobium oxide and the like. The method of the present invention is not particularly limited as long as it is a porous carrier, but the effect is remarkably exhibited in an acidic carrier as compared with the conventional method.
本発明方法で使用される白金属元素としてはパラジウ
ム、ルテニウム、ロジウム、白金、オスミウム、イリジ
ウムがあり、これらの白金族元素化合物としては通常こ
れら白金属元素の塩化物、硝酸塩、金属塩などが用いら
れる。具体的には塩化パラジウム、硝酸パラジウム、塩
化ルテニウム、塩化白金酸等が用いられる。The white metal elements used in the method of the present invention include palladium, ruthenium, rhodium, platinum, osmium, and iridium, and as the platinum group element compounds, chlorides, nitrates, and metal salts of these white metal elements are usually used. To be Specifically, palladium chloride, palladium nitrate, ruthenium chloride, chloroplatinic acid, etc. are used.
担体への白金属元素の担持法としては白金属元素化合物
の水溶液に担体を浸漬させてもよいが、白金属元素化合
物の水溶液をスプレー等で担体に噴霧する方法が好まし
く用いられる。As a method for supporting the white metal element on the carrier, the carrier may be immersed in an aqueous solution of the white metal element compound, but a method of spraying the aqueous solution of the white metal element compound onto the carrier by a spray or the like is preferably used.
担持される白金属元素の量は通常担体1リットル当たり
0.01〜10gであり、好ましくは0.1〜5gの範
囲である。The amount of the white metal element carried is usually 0.01 to 10 g, preferably 0.1 to 5 g per liter of the carrier.
(実施例) 実施例1. 多孔性担体としてシリカアルミナペレット(日揮化学製
N−631HN)を用いた。(Example) Example 1. Silica-alumina pellets (N-631HN manufactured by JGC Chemical Co., Ltd.) were used as the porous carrier.
シリカアルミナペレット100mlを取り、これを500
mlのベンゼン中に室温で1時間浸漬した。1時間後のシ
リカアルミナペレットを取り出し、塩化パラジウム水溶
液(パラジウム濃度37g/1)2.7mlを11mlの純
水で希釈した液をこの担体に噴霧含浸させた。その後ヒ
ドラジンでパラジウムを還元した後150℃で10時間
乾燥して担持触媒を得た。Take 100 ml of silica-alumina pellets and add 500
Immersion in ml of benzene at room temperature for 1 hour. After 1 hour, the silica-alumina pellets were taken out, and a liquid prepared by diluting 2.7 ml of an aqueous palladium chloride solution (palladium concentration: 37 g / 1) with 11 ml of pure water was spray-impregnated into this carrier. After that, palladium was reduced with hydrazine and dried at 150 ° C. for 10 hours to obtain a supported catalyst.
このようにして得られた触媒のパラジウム担持状態をX
線マイクロアナライザーで測定したところパラジウムの
97%以上は担体の表層0.2mm以内に担持されていた。 実施例2〜6、および比較例1〜4 実施例1で用いたベンゼンのかわりに第1表に記載した
化合物に1時間浸漬した後、パラジウムの担持操作を行
い、得られた担持触媒のパラジウム担持状態をX線マイ
クロアナライザーで測定して第1表に記載した結果を得
た。なおベンゼンのかわりに他の化合物を浸漬液として
用いる以外は実施例1と同じ方法で行った。The palladium-supported state of the catalyst thus obtained was determined as X.
When measured by a line microanalyzer, 97% or more of palladium was supported within 0.2 mm of the surface layer of the carrier. Examples 2 to 6 and Comparative Examples 1 to 4 After immersing in the compounds shown in Table 1 for 1 hour instead of benzene used in Example 1, palladium loading operation was carried out to obtain palladium as a supported catalyst. The supported state was measured with an X-ray microanalyzer to obtain the results shown in Table 1. The same procedure as in Example 1 was carried out except that another compound was used as the immersion liquid instead of benzene.
実施例7〜10 実施例1で用いたシリカアルミナのかわりに第2表に記
載した担体100mlを用いてパラジウムの担持操作を行
った。得られた担持触媒のパラジウム担持状態をX線マ
イクロアナライザーで測定し、第2表に記載した結果を
得た。なお担体が異なる以外はすべて実施例1に記載し
たのと同じ方法で行った。 Examples 7 to 10 Instead of the silica-alumina used in Example 1, 100 ml of the carrier described in Table 2 was used to carry out the palladium loading operation. The palladium-supported state of the resulting supported catalyst was measured by an X-ray microanalyzer, and the results shown in Table 2 were obtained. The procedure was the same as that described in Example 1 except that the carrier was different.
実施例11〜14 実施例1で用いた塩化パラジウム水溶液のかわりに第3
表に記載した溶液を用いて白金属元素の担持操作を行っ
た。得られた担持触媒の白金属元素の担持状態をX線マ
イクロアナライザーで測定し第3表に記載した結果を得
た。なお含浸液は金属の担持量が0.1g/1となるよう
に調製した液を14ml用いた。また含浸液が異なる以外
はすべて実施例1に記載したのと同じ方法で行った。 Examples 11 to 14 Third Example Instead of Palladium Chloride Aqueous Solution Used in Example 1
A white metal element was loaded using the solutions listed in the table. The supported state of the white metal element of the obtained supported catalyst was measured by an X-ray microanalyzer, and the results shown in Table 3 were obtained. As the impregnating solution, 14 ml of a solution prepared so that the amount of supported metal was 0.1 g / 1 was used. Further, the same method as described in Example 1 was used except that the impregnating liquid was different.
実施例15 実施例7で用いたのと同じガンマーアルミナペレット1
00mlを500mlのベンゼン中に室温で1時間浸漬し
た。1時間後のガンマーアルミナペレットを取りだし、
次に塩化パラジウム水溶液(パラジウム濃度37g/1)
2.7mlの純水で希釈した液にこの担体を30分間浸漬
した。その後ヒドラジンでパラジウムを還元し、150
℃で10時間乾燥を行い担持触媒を得た。得られた担持
触媒のパラジウム担持状態をX線マイクロアナライザー
で測定したところ、パラジウムは担体の表層0.2mm以内
に96%以上担持されていた。 (発明の効果) 以上の如く、本発明により担体の表層部に簡易に白金属
元素を高比率で担持でき、このように白金属元素を担持
した触媒はヒドラジン、ホルマリン等の還元性液または
水素ガスで還元後、水洗乾燥を行なうことにより水素化
触媒として良好な性能を発揮する触媒となる。 Example 15 Gamma Alumina Pellets 1 Same as Used in Example 7
00 ml was immersed in 500 ml of benzene at room temperature for 1 hour. Take out the gamma-alumina pellet after 1 hour,
Next, aqueous palladium chloride solution (palladium concentration 37g / 1)
This carrier was immersed in a solution diluted with 2.7 ml of pure water for 30 minutes. Then, reduce the palladium with hydrazine,
Drying was carried out at 0 ° C. for 10 hours to obtain a supported catalyst. When the palladium-supported state of the resulting supported catalyst was measured by an X-ray microanalyzer, it was confirmed that 96% or more of the palladium was supported within 0.2 mm of the surface layer of the carrier. (Effects of the Invention) As described above, according to the present invention, the white metal element can be easily supported on the surface layer of the carrier in a high ratio, and the catalyst supporting the white metal element is a reducing liquid such as hydrazine or formalin or hydrogen. After reduction with gas and washing with water and drying, the catalyst can exhibit good performance as a hydrogenation catalyst.
Claims (1)
において、多孔性担体をあらかじめ炭素数5ないし12
の炭化水素化合物に浸漬させた後、白金属元素化合物の
水溶液を含浸させることを特徴とする担持触媒の製造方
法。1. A method of supporting a white metal element on a porous carrier, wherein the porous carrier is preliminarily prepared with a carbon number of 5 to 12.
The method for producing a supported catalyst, which comprises immersing in an aqueous solution of a white metal element compound after being dipped in the hydrocarbon compound of.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60153297A JPH067921B2 (en) | 1985-07-11 | 1985-07-11 | Method for producing supported catalyst |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60153297A JPH067921B2 (en) | 1985-07-11 | 1985-07-11 | Method for producing supported catalyst |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6214943A JPS6214943A (en) | 1987-01-23 |
JPH067921B2 true JPH067921B2 (en) | 1994-02-02 |
Family
ID=15559390
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60153297A Expired - Lifetime JPH067921B2 (en) | 1985-07-11 | 1985-07-11 | Method for producing supported catalyst |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH067921B2 (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102821855B (en) * | 2010-03-29 | 2014-08-27 | 田中贵金属工业株式会社 | Method for production of catalyst having supporting surface |
JP2012108000A (en) * | 2010-11-17 | 2012-06-07 | Toshiba Corp | Catalyst for recombiner of radioactive gaseous waste treatment facility and manufacturing method thereof |
JP6978844B2 (en) * | 2017-03-22 | 2021-12-08 | 岩谷産業株式会社 | Hydrocarbon synthesis catalyst manufacturing method, hydrocarbon manufacturing method |
-
1985
- 1985-07-11 JP JP60153297A patent/JPH067921B2/en not_active Expired - Lifetime
Also Published As
Publication number | Publication date |
---|---|
JPS6214943A (en) | 1987-01-23 |
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