JPS6214943A - Preparation of supported catalyst - Google Patents

Preparation of supported catalyst

Info

Publication number
JPS6214943A
JPS6214943A JP60153297A JP15329785A JPS6214943A JP S6214943 A JPS6214943 A JP S6214943A JP 60153297 A JP60153297 A JP 60153297A JP 15329785 A JP15329785 A JP 15329785A JP S6214943 A JPS6214943 A JP S6214943A
Authority
JP
Japan
Prior art keywords
carrier
compound
palladium
supported
supported catalyst
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.)
Granted
Application number
JP60153297A
Other languages
Japanese (ja)
Other versions
JPH067921B2 (en
Inventor
Yasuhiko Too
東尾 保彦
Toshio Nakayama
敏男 中山
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.)
Sumitomo Chemical Co Ltd
Original Assignee
Sumitomo Chemical 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 Sumitomo Chemical Co Ltd filed Critical Sumitomo Chemical Co Ltd
Priority to JP60153297A priority Critical patent/JPH067921B2/en
Publication of JPS6214943A publication Critical patent/JPS6214943A/en
Publication of JPH067921B2 publication Critical patent/JPH067921B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Exhaust Gas Treatment By Means Of Catalyst (AREA)
  • Catalysts (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)

Abstract

PURPOSE:To enhance catalytic activity by supporting a platinum group element at a high ratio, by immersing a porous carrier in a 5-12C hydrocarbon compound and subsequently impregnating the same with an aqueous solution of a platinum group compound to form a supported catalyst. CONSTITUTION:A porous carrier with surface area of 1-1,000m<2>/g formed of alumina, silica, silica-alumina, magnesia or titania is immersed in a 5-12C hydrocarbon compound and subsequently impregnated with an aqueous solution of a platinum group compound to prepare a supported catalyst. As the aforementioned 5-12C hydrocarbon compound, aliphatic hydrocarbon such as pentane, hexane or octane and alicyclic hydrocarbon such as cyclopentane are used. As the platinum group compound, there are palladium chloride, palladium nitrate, ruthenium chloride and platinic chloride, etc.

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0)への白金
属元素の担持方法に関するものである0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◇ (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
常に速いため触謀り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・ 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0しかしながらこの
方法によると担体に制限があシ、担体の種類によっては
白金属元′Jg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◎ 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47−85670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
48−58980号公報)、ポリエチレングリコ−/L
/l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49−11
4588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54−149891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
素は担体の表層部のみでなく内部にも侵入する場合があ
シ、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0 (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シ除き、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
金属元素化合物Q水溶液を担体に含浸させることによシ
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〇 (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シ、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。
Detailed Description of the Invention (Industrial Application Field) The present invention relates to a method for supporting a platinum metal element on a porous carrier (hereinafter referred to as "carrier").
This relates to a method for manufacturing a supported catalyst in which all or most of a platinum metal element is supported on the surface layer of a support. (Prior art) A supported catalyst in which a platinum metal element is supported on a support is used for hydrogenation reactions of various organic compounds. It is widely used in catalytic conversion reactions, hydrocracking reactions, and catalytic conversion reactions of automobile exhaust gas, but these reactions are generally very fast and proceed on the outer surface of the catalyst, so that the metal inside the catalyst particles is not used effectively. Therefore, when using an expensive platinum metal element as a catalytic material, it is necessary to support the white metal element in a high density on the surface layer of the support for effective use. The method for supporting the metal element is to add an aqueous solution of the platinum element compound to a basic solid oxide carrier or a carrier that has been pretreated to make it basic, and cause hydrolysis by the base on the surface of the carrier to cause the platinum element to be deposited on the surface layer. However, this method has limitations on the carrier, and depending on the type of carrier, the platinum metal base may penetrate into the interior of the carrier, making it impossible to achieve the purpose. A method for adjusting the pH of an aqueous solution of a platinum metal element compound (Japanese Patent Publication No. 47-85670), a method using an acetone solution of a platinum metal element compound as an impregnating liquid (Japanese Patent Application Laid-open No. 48-58980), polyethylene glycol/ L
/l or a method of adding a nonionic surfactant to the impregnating liquid (JP-A-49-111886, JP-A-49-11)
4588) and a method of pre-impregnating a catalyst carrier with a citric acid solution (Japanese Unexamined Patent Publication No. 149891/1989). However, in any of these methods, the platinum metal element may penetrate not only into the surface layer of the carrier but also into the interior thereof, so that the purpose cannot necessarily be achieved. In addition, depending on the method, the catalyst activity may be reduced. The present invention provides a method for supporting a platinum metal element on the surface layer of a carrier very simply and at low cost. That is, all or most of the platinum metal element is supported on the surface layer of the support by first immersing the support in a hydrocarbon compound having 5 to 12 carbon atoms and then impregnating the support with an aqueous solution of the platinum metal element compound Q. (Means for solving the problem) Hydrocarbon compounds having 5 to 12 carbon atoms used in the present invention include aliphatic hydrocarbons such as pentane, hexane, octane, pentene, and hexene. , cyclopentane,
Alicyclic hydrocarbons such as cyclohexane and methylcyclopentane, and aromatic hydrocarbons such as benzene, toluene, xylene and ethylbenzene, preferably 6 carbon atoms.
From 1 to 10 hydrocarbon compounds are used.

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。
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。
Although the conditions for immersing the carrier in the hydrocarbon compound are not particularly limited, the carrier is usually 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1〜100
0 m’/f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 100.
It is a porous carrier of 0 m'/f. Specifically, there are alumina, silica, silica alumina, magnesia, titania, zirconia, 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 more pronounced when using an acidic carrier than in 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、オヌミウム、イリジウ
ムがあシ、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0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0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
The platinum metal elements used in the method of the present invention include palladium, ruthenium, rhodium, platinum, onumium, and iridium, and the compounds of these platinum group elements usually include chlorides, nitrates, metal salts, etc. of these platinum metal elements. Specifically, palladium chloride, palladium nitrate, ruthenium chloride, chloroplatinic acid, etc. are used.As a method for supporting a platinum metal element on a carrier, the carrier may be immersed in an aqueous solution of a platinum element compound. , a method of spraying an aqueous solution of a platinum metal element compound onto the carrier using 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リツトル当たシ
0.01〜10fであシ、好ましくは多孔性担体として
シリカアルミナベレット(8揮化学製N−681HN)
を用いた0シリカアルミナベレツト100mjを取り、
これを500mjのベンゼン中に室温で1時間浸漬した
。1時間後シリカアルミナベレットを取シ出し、塩化パ
ラジウム水溶液(パラジウム濃度87 f/1) 2.
7mJを11mJの純水で希釈した液をこの担体に噴霧
含浸させた。その後ヒドラジノ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。
The amount of platinum metal element supported is usually 0.01 to 10 f per 1 liter of carrier, preferably a silica alumina pellet (N-681HN manufactured by 8 Kiku Kagaku Co., Ltd.) as a porous carrier.
Take 100 mj of 0 silica alumina beret using
This was immersed in 500 mj of benzene at room temperature for 1 hour. After 1 hour, take out the silica alumina pellet and add palladium chloride aqueous solution (palladium concentration 87 f/1) 2.
This carrier was impregnated by spraying with a solution obtained by diluting 7 mJ with 11 mJ of pure water. Thereafter, palladium was reduced with hydrazino 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0.2閣以内に担持されていた
The palladium supported state of the catalyst obtained in this way is
When measured using a wire microanalyzer, more than 97% of the palladium was supported within 0.2 cm of the surface layer of the carrier.

実施例2〜6、および比較例1〜8 実施例1で用いたベンゼンのかわシに第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シ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〇第   1
   表 A:表層0.2■以内に担持されているパラジウムの比
率実施例7〜10 実施例1で用いたシリカアルミナのかわシに第2表に記
載した担体1001117を用いてパラジウムの担持操
作を行った0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0第   2   表 A:表#0.gfi以内に担持されているパラジウムの
比率実施例11〜14 5j!施例1で用いた塩化パラジウム水溶液のかわりに
第8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$8表に記載した結果
を得た0なお含浸液は金属の担持量が0.1 f/1と
なるように調製した液を14tnj用いた〇また含浸液
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・ 実施例15 実施例7で用いたのと同じガンマ−アルミナベレットi
 o OmJを50 OmJのベンゼン中に室温で1時
間浸漬した01時開俵ガンマーアルミナベレットを取シ
だし、次に塩化パラジウム水溶液(パラジウム濃度87
 F/1)2.7mjの純水で希釈した液にとの担体を
80分間浸漬シた0その後とドフジンでパラジウムを還
元し、160℃で10時間乾燥を行い担持触媒を得た0
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0.2 m以内に96%以上担持されていたO (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。
Examples 2 to 6 and Comparative Examples 1 to 8 The benzene wash used in Example 1 was immersed in the compounds listed in Table 1 for 1 hour, and palladium was then supported. The supported state of palladium was measured using an X-ray microanalyzer and the results listed in Table 1 were obtained. 1
Table A: Ratio of palladium supported within 0.2cm of the surface layer Examples 7 to 10 Palladium was supported on the silica alumina glue used in Example 1 using carrier 1001117 listed in Table 2. The state of palladium supported on the obtained supported catalyst was measured using an X-ray microanalyzer, and the results shown in Table 2 were obtained. Table 2 Table A: Table #0 was carried out in the same manner as described in Example 1 except that the carrier was different. Ratio of palladium supported within gfi Examples 11-14 5j! The platinum metal element was supported using the solution listed in Table 8 instead of the palladium chloride aqueous solution used in Example 1. The supported state of the platinum metal element on the obtained supported catalyst was
It was measured with a line microanalyzer and the results listed in the table were obtained. All were performed in the same manner as described in Example 1. Example 15 The same gamma-alumina pellet i used in Example 7.
o OmJ was immersed in 50 OmJ of benzene for 1 hour at room temperature.
F/1) The carrier was immersed in a solution diluted with 2.7 mj of pure water for 80 minutes, and then the palladium was reduced with dofusin and dried at 160°C for 10 hours to obtain a supported catalyst.
When the palladium supported state of the obtained supported catalyst was measured using an X-ray microanalyzer, it was found that 96% or more of palladium was supported within 0.2 m of the surface layer of the support. A high proportion of platinum metal elements can be easily supported on the surface layer of the carrier, and catalysts supported with platinum metal elements in this way can be reduced with hydrogen gas or a reducing liquid such as hydrazine or formalin, and then washed with water and dried to release hydrogen. It becomes a catalyst that exhibits good performance as a chemical catalyst.

Claims (1)

【特許請求の範囲】[Claims] 多孔性担体上に白金属元素を担持する方法において、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。
A method for supporting a platinum metal element on a porous carrier, the supported catalyst being characterized by immersing the porous carrier in advance in a hydrocarbon compound having 5 to 12 carbon atoms, and then impregnating it with an aqueous solution of the platinum metal element compound. manufacturing method.
JP60153297A 1985-07-11 1985-07-11 Method for producing supported catalyst Expired - Lifetime JPH067921B2 (en)

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 true JPS6214943A (en) 1987-01-23
JPH067921B2 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)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4861537B2 (en) * 2010-03-29 2012-01-25 田中貴金属工業株式会社 Method for producing surface-supported catalyst
JP2012108000A (en) * 2010-11-17 2012-06-07 Toshiba Corp Catalyst for recombiner of radioactive gaseous waste treatment facility and manufacturing method thereof
JP2018158279A (en) * 2017-03-22 2018-10-11 岩谷産業株式会社 Hydrocarbon synthesis catalyst, method for producing hydrocarbon synthesis catalyst, hydrocarbon production apparatus, and hydrocarbon production method

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4861537B2 (en) * 2010-03-29 2012-01-25 田中貴金属工業株式会社 Method for producing surface-supported catalyst
JP2012108000A (en) * 2010-11-17 2012-06-07 Toshiba Corp Catalyst for recombiner of radioactive gaseous waste treatment facility and manufacturing method thereof
JP2018158279A (en) * 2017-03-22 2018-10-11 岩谷産業株式会社 Hydrocarbon synthesis catalyst, method for producing hydrocarbon synthesis catalyst, hydrocarbon production apparatus, and hydrocarbon production method

Also Published As

Publication number Publication date
JPH067921B2 (en) 1994-02-02

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