JPH02261542A - Production of metallic catalyst supporting platinum family metal - Google Patents
Production of metallic catalyst supporting platinum family metalInfo
- Publication number
- JPH02261542A JPH02261542A JP8150389A JP8150389A JPH02261542A JP H02261542 A JPH02261542 A JP H02261542A JP 8150389 A JP8150389 A JP 8150389A JP 8150389 A JP8150389 A JP 8150389A JP H02261542 A JPH02261542 A JP H02261542A
- Authority
- JP
- Japan
- Prior art keywords
- metal
- platinum group
- supported
- group metal
- glycol
- 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
Links
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 94
- 239000002184 metal Substances 0.000 title claims abstract description 94
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical compound [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 title claims description 72
- 238000004519 manufacturing process Methods 0.000 title claims description 7
- 239000003863 metallic catalyst Substances 0.000 title abstract 2
- 229910052697 platinum Inorganic materials 0.000 title 1
- 239000007769 metal material Substances 0.000 claims abstract description 29
- 239000003054 catalyst Substances 0.000 claims description 39
- -1 platinum group metal Compound Chemical class 0.000 claims description 17
- 150000001875 compounds Chemical class 0.000 claims description 7
- 239000000126 substance Substances 0.000 claims description 6
- 230000003197 catalytic effect Effects 0.000 abstract description 12
- 150000002334 glycols Chemical class 0.000 abstract description 9
- MTHSVFCYNBDYFN-UHFFFAOYSA-N diethylene glycol Chemical compound OCCOCCO MTHSVFCYNBDYFN-UHFFFAOYSA-N 0.000 description 30
- DNIAPMSPPWPWGF-UHFFFAOYSA-N Propylene glycol Chemical compound CC(O)CO DNIAPMSPPWPWGF-UHFFFAOYSA-N 0.000 description 27
- 229910000953 kanthal Inorganic materials 0.000 description 27
- 239000011259 mixed solution Substances 0.000 description 22
- 230000000052 comparative effect Effects 0.000 description 21
- 238000000034 method Methods 0.000 description 20
- 229920001223 polyethylene glycol Polymers 0.000 description 19
- 239000002202 Polyethylene glycol Substances 0.000 description 18
- 239000000243 solution Substances 0.000 description 15
- ZIBGPFATKBEMQZ-UHFFFAOYSA-N triethylene glycol Chemical compound OCCOCCOCCO ZIBGPFATKBEMQZ-UHFFFAOYSA-N 0.000 description 9
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 8
- 241000264877 Hippospongia communis Species 0.000 description 8
- 239000007864 aqueous solution Substances 0.000 description 8
- 239000000843 powder Substances 0.000 description 8
- UWHCKJMYHZGTIT-UHFFFAOYSA-N Tetraethylene glycol, Natural products OCCOCCOCCOCCO UWHCKJMYHZGTIT-UHFFFAOYSA-N 0.000 description 7
- 239000002253 acid Substances 0.000 description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- LCZVSXRMYJUNFX-UHFFFAOYSA-N 2-[2-(2-hydroxypropoxy)propoxy]propan-1-ol Chemical compound CC(O)COC(C)COC(C)CO LCZVSXRMYJUNFX-UHFFFAOYSA-N 0.000 description 6
- 239000001856 Ethyl cellulose Substances 0.000 description 6
- ZZSNKZQZMQGXPY-UHFFFAOYSA-N Ethyl cellulose Chemical compound CCOCC1OC(OC)C(OCC)C(OCC)C1OC1C(O)C(O)C(OC)C(CO)O1 ZZSNKZQZMQGXPY-UHFFFAOYSA-N 0.000 description 6
- 239000011230 binding agent Substances 0.000 description 6
- 239000000919 ceramic Substances 0.000 description 6
- 238000009713 electroplating Methods 0.000 description 6
- 229920001249 ethyl cellulose Polymers 0.000 description 6
- 235000019325 ethyl cellulose Nutrition 0.000 description 6
- 150000002500 ions Chemical class 0.000 description 6
- 238000002156 mixing Methods 0.000 description 6
- 239000003960 organic solvent Substances 0.000 description 6
- SZXQTJUDPRGNJN-UHFFFAOYSA-N dipropylene glycol Chemical compound OCCCOCCCO SZXQTJUDPRGNJN-UHFFFAOYSA-N 0.000 description 5
- 239000010419 fine particle Substances 0.000 description 5
- 238000010438 heat treatment Methods 0.000 description 5
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 4
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 4
- 238000000746 purification Methods 0.000 description 4
- HZAXFHJVJLSVMW-UHFFFAOYSA-N 2-Aminoethan-1-ol Chemical compound NCCO HZAXFHJVJLSVMW-UHFFFAOYSA-N 0.000 description 3
- 238000007084 catalytic combustion reaction Methods 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 230000003287 optical effect Effects 0.000 description 3
- 239000011148 porous material Substances 0.000 description 3
- 238000005303 weighing Methods 0.000 description 3
- PIICEJLVQHRZGT-UHFFFAOYSA-N Ethylenediamine Chemical compound NCCN PIICEJLVQHRZGT-UHFFFAOYSA-N 0.000 description 2
- 150000001412 amines Chemical class 0.000 description 2
- 238000007664 blowing Methods 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 229910052593 corundum Inorganic materials 0.000 description 2
- 239000010431 corundum Substances 0.000 description 2
- 239000003344 environmental pollutant Substances 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 150000002739 metals Chemical class 0.000 description 2
- 235000019645 odor Nutrition 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N palladium Substances [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 231100000719 pollutant Toxicity 0.000 description 2
- 239000010948 rhodium Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003836 solid-state method Methods 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- FZZMTSNZRBFGGU-UHFFFAOYSA-N 2-chloro-7-fluoroquinazolin-4-amine Chemical compound FC1=CC=C2C(N)=NC(Cl)=NC2=C1 FZZMTSNZRBFGGU-UHFFFAOYSA-N 0.000 description 1
- CNPURSDMOWDNOQ-UHFFFAOYSA-N 4-methoxy-7h-pyrrolo[2,3-d]pyrimidin-2-amine Chemical compound COC1=NC(N)=NC2=C1C=CN2 CNPURSDMOWDNOQ-UHFFFAOYSA-N 0.000 description 1
- 150000007513 acids Chemical class 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 150000001298 alcohols Chemical class 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 229910010293 ceramic material Inorganic materials 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000000151 deposition Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000008187 granular material Substances 0.000 description 1
- WGCNASOHLSPBMP-UHFFFAOYSA-N hydroxyacetaldehyde Natural products OCC=O WGCNASOHLSPBMP-UHFFFAOYSA-N 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- GPNDARIEYHPYAY-UHFFFAOYSA-N palladium(ii) nitrate Chemical compound [Pd+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O GPNDARIEYHPYAY-UHFFFAOYSA-N 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- VXNYVYJABGOSBX-UHFFFAOYSA-N rhodium(3+);trinitrate Chemical compound [Rh+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O VXNYVYJABGOSBX-UHFFFAOYSA-N 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000002904 solvent Substances 0.000 description 1
- 238000005507 spraying Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
Landscapes
- Catalysts (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、線状、網状、板状、ハニカム状、リング状な
どの形状を有する金属材料に白金族金属を担持した白金
族金属担持金属触媒の製造方法に関する。[従来の技術
]
白金族金属を担持した触媒は、各種の酸化特性について
低温で優れた触媒活性を示すため、工場及び自動車等か
ら排出される各種公害汚染物質及び悪臭の浄化に利用さ
れてきl;。従来、この白金族金属担持触媒としては、
セラミックの担体(ハニカム、球、顆粒、ベレット等)
に白金族金属を担持したアルミナ等の微粒子をウォッシ
ュコートした物が用いられてきた。Detailed Description of the Invention [Industrial Application Field] The present invention relates to a platinum group metal-supported metal in which a platinum group metal is supported on a metal material having a linear, net-like, plate-like, honeycomb-like, or ring-like shape. The present invention relates to a method for producing a catalyst. [Prior Art] Catalysts supporting platinum group metals exhibit excellent catalytic activity at low temperatures for various oxidation properties, and are therefore used to purify various pollutants and bad odors discharged from factories, automobiles, etc. ;. Conventionally, as this platinum group metal supported catalyst,
Ceramic carriers (honeycombs, spheres, granules, pellets, etc.)
A material wash-coated with fine particles of alumina or the like supporting a platinum group metal has been used.
ところで、最近では、定常状態での各種公害物質及び悪
臭の浄化だけでなく、定常状態に至る昇温時での浄化性
能が問題となってきた。また、使用温度自体の低温化も
クローズアップされてきた。Incidentally, recently, not only the purification of various pollutants and bad odors in a steady state, but also the purification performance when the temperature is raised to reach a steady state has become a problem. Also, attention has been focused on lowering the operating temperature itself.
これらの問題を解決する手段として、触媒自体の暖まり
を速めることが考えられた。そのために、まず、担体の
切り替え、具体的には、従来使われてきた熱容量の大き
なセラミックから熱容量の小さな金属材料への切り替え
が注目を集めるようになった。As a means to solve these problems, it was considered to speed up the warming of the catalyst itself. To this end, switching the carrier, specifically, switching from the traditionally used ceramic material with a large heat capacity to a metal material with a small heat capacity, has started to attract attention.
しかし、金属材料に白金族金属を担持したアルミナ等の
微粒子をウォッシュコートしたため、アルミナ等の微粒
子に熱を奪われ、昇温時での浄化特性及び浄化特性の低
温化は満足できるものではなかった。また、金属材料と
アルミナ等の微粒子の密着性の悪さも問題になった。However, because the metal material was wash-coated with fine particles such as alumina that supported platinum group metals, heat was taken away by the fine particles such as alumina, and the purification characteristics at elevated temperatures and the purification characteristics at low temperatures were not satisfactory. . Another problem was the poor adhesion between metal materials and fine particles such as alumina.
そこで、金属材料に直接、白金族金属を担持することに
より、触媒の暖まりを速めるとか考えられた。このよう
な線状、網状、板状、ハニカム状、リング状などの形状
を有する金属上に白金族金属を表面コーティングする方
法として、特開昭53113292号公報及び特開昭5
8−159848号公報に、電気メツキ法が開示されて
いる。Therefore, it was thought that supporting a platinum group metal directly on a metal material would speed up the warming of the catalyst. As a method for surface coating a platinum group metal on a metal having such a linear, net-like, plate-like, honeycomb-like, ring-like shape, etc., Japanese Patent Application Laid-Open No. 53113292 and Japanese Patent Application Laid-open No. 5311329 are disclosed.
8-159848 discloses an electroplating method.
また、その他に、白金族金属の塩を水、酸、またはアル
コール等に溶解させた後、目的とする金属上に付着させ
、それを加熱・分解したり化学的な還元によって金属を
析出させるイオン法と白金族金属粉を接着剤と共に目的
とする金属上に付着後焼成する固体法とがあった。In addition, ions can be used to precipitate metals by dissolving platinum group metal salts in water, acids, alcohols, etc., depositing them on the target metal, and heating and decomposing them or chemically reducing them. There are two methods: the solid state method, in which platinum group metal powder is deposited on the target metal together with an adhesive, and then fired.
しかし、これらの方法にいずれも一長一短があった。電
気メツキ法及びイオン法では、目的とする金属との密着
性に優れた触媒を形成し易いが、その反面、白金族金属
の有効表面積が少なくなり易く、触媒活性が劣る傾向に
あった。一方、固体法では、最初から目的に合った粒径
、幾何学的形状を有する粉体を選べるので、電気メツキ
及びイオン法に比べて白金族金属の有効表面積を大きく
し易いが目的とする金属との密着性に乏しい傾向にあっ
た。However, each of these methods had advantages and disadvantages. In the electroplating method and the ion method, it is easy to form a catalyst with excellent adhesion to the target metal, but on the other hand, the effective surface area of the platinum group metal tends to decrease, and the catalytic activity tends to be poor. On the other hand, in the solid-state method, it is possible to select powder with a particle size and geometric shape that suit the purpose from the beginning, so it is easier to increase the effective surface area of the platinum group metal compared to electroplating and ion methods. They tended to have poor adhesion.
これらの欠点を補うために、特開昭59−123535
号公報に、モノエタノールアミン、エチレンジアミン等
の有機溶剤中に白金族金属の微粉末及びそのイオンを共
存させてエチルセルロースのカルピトール水溶液等の有
機バインダーを加えた混合溶液をセラミックハニカム担
体等に付着させた後、加熱・焼成処理することを特徴と
する白金族金属触媒の担持方法が開示されている。In order to compensate for these shortcomings, Japanese Patent Application Laid-Open No. 59-123535
In the publication, a mixed solution in which fine powder of a platinum group metal and its ions were made to coexist in an organic solvent such as monoethanolamine or ethylenediamine, and an organic binder such as an aqueous solution of calpitol of ethyl cellulose was added was attached to a ceramic honeycomb carrier, etc. A method for supporting a platinum group metal catalyst is disclosed, which is characterized in that the catalyst is then heated and calcined.
[本発明が解決しようとする問題点]
まず、特開昭53−113292号公報及び特開昭58
−159848号公報に開示されている電気メツキ法は
、どのような形状の金属表面でも均一に白金族金属をコ
ーティングでき、且つ、金属との密着性にも優れている
ので、外観だけの判断では理想的な形状を示していた。[Problems to be solved by the present invention] First, Japanese Patent Application Laid-Open No. 53-113292 and Japanese Patent Application Laid-open No. 58
The electroplating method disclosed in Publication No. 159848 can coat metal surfaces of any shape with platinum group metal uniformly, and has excellent adhesion to metals, so it is difficult to judge by appearance alone. It had an ideal shape.
しかし、実際の触媒活性という面では、後述するように
著しく劣っており、数回の着火試験で触媒活性を失って
しまい、実用にはまったく適さなかった。However, in terms of actual catalytic activity, as will be described later, it was significantly inferior, losing catalytic activity after several ignition tests, and was completely unsuitable for practical use.
次に、特開昭59−123535号公報に開示されてい
るモノエタノールアミン、エチレンジアミン等の有機溶
剤中に白金族金属の微粉末及びそのイオンを共存させて
エチルセルロースのカルピトール水溶液等の有機バイン
ダーを加えた混合溶液を担体に付着させた後、加熱・焼
成処理する方法も、同公報中の実施例に挙げたように、
表面に直径数ミクロン前後のマクロなポアーが数多く開
いているセラミックハニカムには有効であったかもじれ
ないが、線状、網状、板状、ハニカム状、リング状など
の形状を有する金属材料のようにその表面がセラミック
に比べてミクロなポアーすらほとんどない場合には、予
め共存させている白金族金属の微粉末が担持後の白金族
金属の剥離を誘発する恐れがあり、バインダーの選択が
非常に重要になる。実際、後述するように、同公報に開
示されているエチルセルロースのカルピトール水溶液の
有機バインダーでは白金族金属の剥離を防止することは
できなかった。Next, a fine powder of a platinum group metal and its ions are made to coexist in an organic solvent such as monoethanolamine or ethylenediamine as disclosed in JP-A-59-123535, and an organic binder such as an aqueous solution of calpitol of ethyl cellulose is added. As mentioned in the examples in the same publication, there is also a method of applying a mixed solution to a carrier and then heating and baking it.
It may have been effective for ceramic honeycombs, which have many macroscopic pores with a diameter of several microns on the surface, but it may be effective for ceramic honeycombs, which have many macroscopic pores with a diameter of several microns on the surface, but it may be effective for metal materials with shapes such as lines, nets, plates, honeycombs, and rings. If the surface has almost no microscopic pores compared to ceramic, there is a risk that the fine powder of platinum group metal coexisting in advance may cause the platinum group metal to peel off after being supported, so the selection of the binder is very difficult. becomes important. In fact, as will be described later, the organic binder of the aqueous solution of ethyl cellulose in calpitol disclosed in the publication was unable to prevent the platinum group metal from peeling off.
更に、同公報に開示されている方法では白金族金属の担
持量がセラミックハニカムに対して0゜2重量%程度し
かなく、白金族金属の剥離無しに数〜十数重量%もの白
金族金属を担持することは極めて困難であると思われた
。実際、後述するように、金属担体に白金族金属を担持
する場合に、同公報に開示されている方法では大半の白
金族金属が剥離してしまい、金属担体上に残っている白
金族金属の量はコンマ数%以下であった。Furthermore, in the method disclosed in the same publication, the amount of platinum group metal supported on the ceramic honeycomb is only about 0.2% by weight, and it is possible to carry several to several tens of weight% of platinum group metal without peeling off the platinum group metal. It seemed extremely difficult to carry it. In fact, as will be described later, when platinum group metals are supported on a metal carrier, most of the platinum group metals are peeled off using the method disclosed in the same publication, and the remaining platinum group metals on the metal carrier are removed. The amount was less than a few tenths of a percent.
このため、線状、網状、板状、ハニカム状、すング状な
との形状を有する金属材料との密着性に優れ、触媒活性
が高く、しかも、数〜十数重量%もの白金族金属でも一
度で担持できる白金族金属担持金属触媒の製造方法が求
められていた。For this reason, it has excellent adhesion to metal materials with linear, net, plate, honeycomb, and ring shapes, and has high catalytic activity. There has been a need for a method for producing a platinum group metal-supported metal catalyst that can be supported in one step.
[本発明の目的]
本発明は、線状、網状、板状、ハニカム状、リング状な
どの形状を有する金属材料との密着性に優れ、触媒活性
が高く、しかも、数〜十数重量%もの白金族金属を一度
で担持できる白金族金属担持金属触媒の製造方法を提供
することを目的とする。[Objective of the present invention] The present invention has excellent adhesion to metal materials having shapes such as linear, net-like, plate-like, honeycomb-like, and ring-like shapes, has high catalytic activity, and has a content of several to several tens of percent by weight. An object of the present invention is to provide a method for producing a platinum group metal-supported metal catalyst that can support a platinum group metal at once.
[問題点を解決するための手段1
本発明者は、各種有機溶媒の中で、下記式%式%)
式中、RはH又はCH,を表わし、
RがHであるときは、n≧2であり、
RがCH,であるときは、n≧1である、で表わされる
化合物(グリコール類)からなる群より選択した1種ま
たは2種以上の化合物、たとえばジエチレングリコール
、トリエチレングリコール、テトラエチレングリコール
、ポリエチレングリコール、プロピレングリコール、ジ
グロヒレングリコーノ呟トリプロピレングリコールカ線
状、網状、板状、ハニカム状、リング状などの形状を有
する金属材料との密着性に優れ、触媒活性が高く、しか
も、数〜十数重量%もの白金族金属を一度で担持できる
白金族金属担持金属触媒を製造するための有効な物質で
あることを見いだし、本発明を完成させた。本発明の目
的は、線状、網状、板状、ハニカム状、リング状などの
形状を有する金属材料に白金族金属を担持した白金族金
属担持金属触媒の製造方法において、白金族金属の化合
物と上記グリコール類の少なくとも一つを含む溶液を金
属材料に付着させた後、該金属、材料を熱処理すること
を特徴とする白金族金属担持金属触媒の製造方法により
達成される。[Means for Solving the Problems 1] The present inventor has found that among various organic solvents, the following formula % formula %) In the formula, R represents H or CH, and when R is H, n≧ 2, and when R is CH, n≧1, one or more compounds selected from the group consisting of compounds (glycols), such as diethylene glycol, triethylene glycol, tetra Ethylene glycol, polyethylene glycol, propylene glycol, tripropylene glycol has excellent adhesion to metal materials with shapes such as linear, net, plate, honeycomb, and ring shapes, and has high catalytic activity. Moreover, they have discovered that it is an effective substance for producing a platinum group metal-supported metal catalyst that can support several to tens of weight percent of platinum group metal at once, and have completed the present invention. An object of the present invention is to provide a method for producing a platinum group metal-supported metal catalyst in which a platinum group metal is supported on a metal material having a linear, net-like, plate-like, honeycomb-like, or ring-like shape. This is achieved by a method for producing a platinum group metal-supported metal catalyst, which comprises applying a solution containing at least one of the above glycols to a metal material, and then heat-treating the metal or material.
以下、本発明の詳細な説明する。The present invention will be explained in detail below.
本発明に用いられる上記グリコール類の中で、ポリエチ
レングリコールは平均分子量が200以上の物を差す。Among the above glycols used in the present invention, polyethylene glycol refers to those having an average molecular weight of 200 or more.
この内、平均分子量が200〜400のポリエチレング
リコールは室温で液体であるので、そのまま溶液として
使用するこができる。Among these, polyethylene glycol having an average molecular weight of 200 to 400 is liquid at room temperature, so it can be used as it is as a solution.
平均分子量が600以上のポリエチレングリコールは、
室温では分子量が増すに従って外観が半固体(平均分子
量;600)、白色軟質ワックス状(平均分子量; 1
000前後)、乳白色ロウ状固体(平均分子量; 30
00以上)になるが、いずれも水に良く溶けるので水に
溶かした後、溶液として使用することができる。ジエチ
レングリコール、トリエチレングリコール、テトラエチ
レングリコール、プロピレングリコール、ジプロピレン
グリコール、トリエチレングリコールハいスレも室温で
液体であるので、そのまま溶液として使用することがで
きる。Polyethylene glycol with an average molecular weight of 600 or more is
At room temperature, as the molecular weight increases, the appearance changes from semi-solid (average molecular weight: 600) to white soft wax-like (average molecular weight: 1
000), milky white waxy solid (average molecular weight; 30
00 or more), but since they all dissolve well in water, they can be used as a solution after being dissolved in water. Diethylene glycol, triethylene glycol, tetraethylene glycol, propylene glycol, dipropylene glycol, and triethylene glycol are also liquid at room temperature, so they can be used as they are as a solution.
本発明で用いられる白金族金属については、上記グリコ
ール類、たとえばジエチレングリコーノ呟トリエチレン
グリコール、テトラエチレングリコール、ポリエチレン
グリコール、プロピレングリコール、ジプロピレングリ
コール、トリプロピレングリコールがいずれも水、アル
コール等の有機溶剤に良く溶けるので、白金族金属の種
類は特に問わず、その化合物も水、アルコール等の有機
溶剤に可溶であれば何でもかまわない。Regarding the platinum group metal used in the present invention, the above-mentioned glycols, such as diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, and tripropylene glycol, are all suitable for use with water, alcohol, etc. Since it is well soluble in solvents, the type of platinum group metal is not particularly important, and any compound thereof may be used as long as it is soluble in organic solvents such as water and alcohol.
また、白金族金属の化合物を溶かした溶液と上記グリコ
ール類、たとえばジエチレングリコーノ呟トリエチレン
グリコール、テトラエチレングリコ−)し、ポリエチレ
ングリコール、プロピレングリコール、ジプロピレング
リコール、トリプロピレングリコールの少なくとも一つ
を含む溶液とを混ぜ合わせた際、白金族金属及び/また
はその化合物の微粒子が生成してもかまわない。Alternatively, a solution containing a platinum group metal compound and the above glycols (for example, diethylene glycol, triethylene glycol, tetraethylene glycol), and at least one of polyethylene glycol, propylene glycol, dipropylene glycol, and tripropylene glycol are added. When mixed with a solution containing the metal, fine particles of the platinum group metal and/or its compound may be generated.
水、アルコール等の有機溶剤に溶解させる白金族金属の
化合物の量についても金属材料上に担持する白金族金属
の量に応じて飽和するまで加えることができる。白金族
金属の化合物を溶かした水、アルコール等の有機溶剤と
上記グリコール類、たとえばジエチレングリコール、ト
リエチレングリコール、テトラエチレングリコール、ポ
リエチレングリコール呟 プロピレングリコール、ジブ
ロビレンクリコール、トリエチレングリコールノ少なく
とも一つを含む溶液との混合比率は特に問わないが、粘
度を適度に保つため、及び、白金族金属を金属表面に均
一に担持するために、重量比でl/10〜50/l、好
ましくは1/7〜30/1、より好ましくは115〜2
0/lであることが望ましい。The amount of the platinum group metal compound to be dissolved in an organic solvent such as water or alcohol can be added until saturation is achieved depending on the amount of platinum group metal supported on the metal material. Water in which a platinum group metal compound is dissolved, an organic solvent such as alcohol, and at least one of the above glycols, such as diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, propylene glycol, dibrobylene glycol, and triethylene glycol. The mixing ratio with the solution is not particularly limited, but in order to maintain an appropriate viscosity and to uniformly support the platinum group metal on the metal surface, the weight ratio is l/10 to 50/l, preferably 1/l. 7-30/1, more preferably 115-2
It is desirable that the ratio is 0/l.
金属材料の材質は特に問わないが、使用条件上、高温に
さらされることが多いので、耐熱性の高いものが望まし
い。Although the quality of the metal material is not particularly limited, it is desirable that it has high heat resistance since it is often exposed to high temperatures due to usage conditions.
金属材料の前処理は特に必要としないが、白金族金属を
金属表面に均一に担持するため、予め、金属材料を酸等
に浸すことにより化学的に処理するか、コランダム等の
微粉末を圧縮空気と共に吹き付けることにより物理的に
処理することにより金属表面を荒らすか、または、10
00°C以上の高温で数分から数時間熱処理することに
よりウィスカーを生やして金属表面を凹凸にするほうが
好ましい。Pretreatment of the metal material is not particularly required, but in order to uniformly support the platinum group metal on the metal surface, the metal material may be chemically treated by soaking it in acid, etc., or fine powder such as corundum may be compressed. Roughen the metal surface by physically treating it by blowing with air or
It is preferable to heat the metal surface at a high temperature of 00° C. or higher for several minutes to several hours to generate whiskers and make the metal surface uneven.
金属材料からの白金族金属の剥離を防ぐために行う、白
金族金属の化合物及び上記グリコール類、たとえばジエ
チレングリコール、トリエチレングリコール、テトラエ
チレングリコール、ポリエチレングリコール、プロピレ
ングリコール、ジプロピレングリコール、トリプロピレ
ングリコールの少なくとも一つを含んだ混合溶液を付着
させた後の熱処理温度は、400°C−1100°C1
より好ましくは600°C〜900°Cが望ましい。こ
の範囲以下の温度では白金族金属の化合物が白金族金属
及び/またはその酸化物になりにくいし、この範囲以上
の温度では金属材料自体がその温度に耐えられない。ま
た、熱処理時間は、1分〜3時間、好ましくは3分〜2
時間、より好ましくは5分〜1時間が望ましい。At least a platinum group metal compound and the above-mentioned glycols, such as diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, propylene glycol, dipropylene glycol, and tripropylene glycol, in order to prevent the platinum group metal from peeling off from the metal material. The heat treatment temperature after attaching the mixed solution containing one is 400°C-1100°C1
More preferably, the temperature is 600°C to 900°C. At temperatures below this range, compounds of platinum group metals are difficult to convert into platinum group metals and/or their oxides, and at temperatures above this range, the metal material itself cannot withstand the temperatures. The heat treatment time is 1 minute to 3 hours, preferably 3 minutes to 2 hours.
Time, more preferably 5 minutes to 1 hour.
以下、本発明方法を実施例により、さらに詳細に説明す
るが、本発明方法はこれらの実施例により限定されるも
のではない。Hereinafter, the method of the present invention will be explained in more detail with reference to Examples, but the method of the present invention is not limited to these Examples.
使用する金属材料の形状としては、−例として、担持さ
れた白金族金属が最も剥離し易い金網を選んだ。また、
材質としては、熱耐久性の高いカンタルを選んだ。As for the shape of the metal material used, for example, a wire mesh from which the supported platinum group metal is most easily peeled off was selected. Also,
As for the material, Kanthal, which has high thermal durability, was selected.
実施例1
水酸化白金酸をモノエタノールアミンに溶かした溶液(
Pt濃度;20重量%)Igをメスピペットにて採取し
、20m12ビーカーに入れた。ポリエチレングリコー
ル(平均分子量; 400) 0.5gをメスピペット
にて採取し、上記ビーカーに加えた。両者を筆で良く混
合した後、30メツシユ、4cm角のカンタル金網(1
100°Cで3時間熱処理済み)に筆でこの混合溶液を
両面に隅無く塗り付けた。混合溶液を塗り付けたカンタ
ル金属をマツフル炉内で700°C130分間焼成した
。ptの担持量は7重量%(2mg/ cm2)であっ
た。Example 1 A solution of hydroxyplatinic acid dissolved in monoethanolamine (
Pt concentration: 20% by weight) Ig was collected using a graduated pipette and placed in a 20m12 beaker. 0.5 g of polyethylene glycol (average molecular weight: 400) was collected with a measuring pipette and added to the beaker. After mixing both well with a brush, add 30 mesh, 4 cm square Kanthal wire mesh (1
This mixed solution was applied with a brush to both sides of the substrate (which had been heat treated at 100°C for 3 hours) without any corners. The Kanthal metal coated with the mixed solution was fired in a Matsufuru furnace at 700°C for 130 minutes. The amount of PT supported was 7% by weight (2 mg/cm2).
実施例2
実施例1と同じ方法で調製した混合溶液を30メツシユ
、4cm角のカンタル金網(コランダム等の微粉末を圧
縮空気と共に吹き付は処理済み)に筆で両面に隅無く塗
り付けた後、マツフル炉内で700°C130分間焼成
した。Ptの担持量は7重量%(2mg/am”)であ
った。Example 2 After applying 30 meshes of the mixed solution prepared in the same manner as in Example 1 to a 4 cm square Kanthal wire mesh (spraying of fine powder such as corundum with compressed air has already been done) on both sides with a brush, without any corners. , and baked in a Matsufuru furnace at 700°C for 130 minutes. The amount of Pt supported was 7% by weight (2 mg/am'').
実施例3
実施例1と同じ方法で調製した混合溶液を30メツシユ
、4cm角のカンタル金網(未処理)に筆で両面に隅無
く塗り付けた後、マツフル炉内で700°C130分間
焼成した。ptの担持量は7重量%(2mg/cm2)
であった。Example 3 A mixed solution prepared in the same manner as in Example 1 was applied to 30 meshes of 4 cm square Kanthal wire mesh (untreated) with a brush on both sides without corners, and then baked in a Matsufuru furnace at 700°C for 130 minutes. The supported amount of pt is 7% by weight (2mg/cm2)
Met.
実施例4
ポリエチレングリコール(平均分子量;400)の代り
にジエチレングリコールを同じ量用い、実施例1と同じ
方法で調製した混合溶液を30メツシユ、4cm角のカ
ンタル金網(110o0cで3時間熱処理済み)に筆で
両面に隅無く塗り付けた後、マツフル炉内で700°C
130分間焼成した。Example 4 Using the same amount of diethylene glycol instead of polyethylene glycol (average molecular weight: 400), a mixed solution prepared in the same manner as in Example 1 was brushed onto a 30 mesh, 4 cm square Kanthal wire mesh (heat treated at 110°C for 3 hours). After coating both sides without corners, heat in a Matsufuru furnace at 700°C.
It was baked for 130 minutes.
Ptの担持量は5重量%(1−5mg/ cm2) テ
あっtこ。The supported amount of Pt is 5% by weight (1-5mg/cm2).
実施例5
ポリエチレングリコール(平均分子量;400)の代り
にプロピレングリコールを同じ量用い、実施例1と同じ
方法で調製した混合溶液を30メツシユ、4cm角のカ
ンタル金網(l100’c!で3時間熱処理済み)に筆
で両面に隅無く塗り付けた後、マツフル炉内で700°
C130分間焼成した。Example 5 Using the same amount of propylene glycol instead of polyethylene glycol (average molecular weight: 400), a mixed solution prepared in the same manner as in Example 1 was heat-treated with 30 meshes and a 4 cm square Cantal wire mesh (1100'C!) for 3 hours. After applying it on both sides with a brush without any corners, heat it at 700° in a Matsufuru furnace.
It was fired for C130 minutes.
Ptの担持量は3.3重量%(1mg/am2)であっ
た。The amount of Pt supported was 3.3% by weight (1 mg/am2).
実施例6
ポリエチレングリコール(平均分子量;400)の代り
にジプロピレングリコールを同じ量用い、実施例1と同
じ方法で調製した混合溶液を30メツシユ、4cm角の
カンタル金網(llOoocで3時間熱処理済み)に筆
で両面に隅無く塗り付けた後、マツフル炉内で700℃
、30分間焼成した。Example 6 Using the same amount of dipropylene glycol instead of polyethylene glycol (average molecular weight: 400), a mixed solution prepared in the same manner as in Example 1 was applied to 30 meshes of 4 cm square Kanthal wire mesh (heat treated with llOooc for 3 hours). After applying it on both sides with a brush without any corners, heat it in a Matsufuru oven at 700℃.
, and baked for 30 minutes.
Ptの担持量は13i1量%(4mg/ cm’) テ
あツタ。The amount of Pt supported was 1% (4 mg/cm') of 13i.
実施例7
ポリエチレングリコール(平均分子量、400)の代り
にトリプロピレングリコールを同じ量用い、実施例1と
同じ方法で調製した混合溶液を30メツシユ、4cm角
のカンタル金網(11”oooCで3時間熱処理済み)
に筆で両面に隅無く塗り付けた後、マツフル炉内で70
0°C130分間焼成した。Example 7 Using the same amount of tripropylene glycol instead of polyethylene glycol (average molecular weight, 400), a mixed solution prepared in the same manner as in Example 1 was heated to 30 mesh, 4 cm square Kanthal wire mesh (11" oooC for 3 hours) completed)
After applying it on both sides with a brush without any corners, heat it in a Matsufuru oven for 70 minutes.
It was baked at 0°C for 130 minutes.
Ptの担持量は13重量%(4mg/cm”)であった
。The amount of Pt supported was 13% by weight (4 mg/cm'').
実施例8
水酸化白金酸のアミン溶液(Pt濃度;20重量%)I
gをメスピペットにて採取し、20m12ビーカーに入
れた。ジエチレングリコール0.25gをメスピペット
にて採取し、上記ビーカーに加えた。ポリエチレングリ
コール(平均分子量;400)0.25gをメスピペッ
トにて採取し、上記ビーカーに加えた。3種類の溶液を
筆で良く混合した後、30メツシユ、4crn角のカン
タル金網(1100°Cで3時間熱処理済み)に筆で混
合溶液を両面に隅無く塗り付けた。混合溶液を塗り付け
たカンタル金網をマツフル炉内で700℃、30分間焼
成した。Ptの担持量は17重量%(5mg/cが)で
あった。Example 8 Amine solution of hydroxyplatinic acid (Pt concentration: 20% by weight) I
g was collected with a measuring pipette and placed in a 20 m12 beaker. 0.25 g of diethylene glycol was collected with a measuring pipette and added to the beaker. 0.25 g of polyethylene glycol (average molecular weight: 400) was collected with a measuring pipette and added to the beaker. After thoroughly mixing the three types of solutions with a brush, the mixed solution was applied with a brush to both sides of a 30 mesh, 4 crn square Kanthal wire mesh (heat treated at 1100° C. for 3 hours) without any corners. The Kanthal wire mesh coated with the mixed solution was fired in a Matsufuru furnace at 700°C for 30 minutes. The amount of Pt supported was 17% by weight (5 mg/c).
実施例9
硝酸パラジウムの水溶液(Pd濃度;20重量%)Ig
をメスピペットにて採取し、20m4ビーカーに入れた
。ポリエチレングリコール(平均分子量; 400)0
.5gをメスピペットにて採取し、上記ビーカーに加え
た。両者を筆で良く混合した後、30メツシユ、4cm
角のカンタル金網(1100°Cで3時間熱処理済み)
に筆で混合溶液を両面に隅無く塗り付けた。混合溶液を
塗り付けたカンタル金網をマツフル炉内で700°C!
、30分間焼成した。Pdの担持量は7重量%(2mg
/ cmってあった。Example 9 Aqueous solution of palladium nitrate (Pd concentration: 20% by weight) Ig
was collected with a graduated pipette and placed in a 20m4 beaker. Polyethylene glycol (average molecular weight; 400) 0
.. 5 g was collected with a measuring pipette and added to the beaker. After mixing both well with a brush, 30 meshes, 4 cm
Corner Kanthal wire mesh (heat treated at 1100°C for 3 hours)
The mixed solution was applied to both sides with a brush without any corners. Kanthal wire mesh coated with the mixed solution is heated to 700°C in a Matsufuru furnace!
, and baked for 30 minutes. The supported amount of Pd was 7% by weight (2mg
/ cm.
実施例IO
硝酸ロジウムの水溶液(Rh濃度:1o重量%)Igを
メスピペットにて採取し、20mQビーカーに入れた。Example IO An aqueous solution of rhodium nitrate (Rh concentration: 10% by weight) Ig was collected with a measuring pipette and placed in a 20 mQ beaker.
ポリエチレングリコール(平均分子量; 400)0.
5gをメスピペットにて採取し、上記ビーカーに加えた
。両者を筆で良く混合した後、30メツシユ、4cm角
のカンタル金網(1100°Cで3時間熱処理済み)に
筆で混合溶液を両面に隅無く塗り付けた。混合溶液を塗
り付けたカンタル金網をマツフル炉内で7oo℃、30
分間焼成した。Rhの担持量は3.3重量%(1mg/
0m2)であった。Polyethylene glycol (average molecular weight: 400) 0.
5 g was collected with a measuring pipette and added to the beaker. After thoroughly mixing both with a brush, the mixed solution was applied to both sides of a 30-mesh, 4 cm square Kanthal wire mesh (heat-treated at 1100° C. for 3 hours) without any corners using a brush. The Kanthal wire mesh coated with the mixed solution was heated in a Matsufuru furnace at 70°C and 30°C.
Bake for a minute. The amount of Rh supported was 3.3% by weight (1mg/
0m2).
比較例1
30メツシユ、4cm角のカンタル金網(1100°C
で3時間熱処理済み)にptを電気メツキした。ptの
担持量は10重量%(3mg/cm”)であった。Comparative Example 1 30 mesh, 4 cm square Kanthal wire mesh (1100°C
(heat treated for 3 hours) was electroplated with PT. The amount of pt supported was 10% by weight (3 mg/cm'').
比較例2
水酸化白金酸のアミン溶液(Pt濃度:2o重量%)I
gをメスピペットにて採取し、20mffビーカーに入
れた。エチルセルロースのカルピトール水溶液0.5g
をメスピペットにて採取し、上記ビーカーに加えた。両
者を筆で良く混合し、Pもの微粒子が数多く生成したの
を確認した後、3゜メツシュ、4cm角のカンタル金網
(lloO’c!で3時間熱処理済み)に筆で混合溶液
を両面に隅無く塗り付けた。混合溶液を塗り付けたカン
タル金網をマツフル炉内で700 ’C130分間焼成
した。Comparative Example 2 Amine solution of hydroxyplatinic acid (Pt concentration: 2o wt%) I
g was collected with a measuring pipette and placed in a 20 mff beaker. Calpitol aqueous solution of ethylcellulose 0.5g
was collected with a measuring pipette and added to the beaker. Mix both well with a brush, and after confirming that a large number of P particles have been generated, apply the mixed solution on both sides of a 3° mesh, 4 cm square Kanthal wire mesh (heat treated with lloO'c! for 3 hours) using a brush. I painted it without any problem. The Kanthal wire mesh coated with the mixed solution was fired in a Matsufuru furnace at 700'C for 130 minutes.
金網をそっと持ち上げて秤量した結果、Ptの担持量は
3.3重量%(1mg/ am”) テあツタ。As a result of gently lifting the wire mesh and weighing it, the amount of Pt supported was 3.3% by weight (1 mg/am'').
比較例3
水酸化白金酸のアミン溶液(Pt濃度;20重量%)I
gをメスピペットにて採取し、2o−ビーカーに入れた
。エチレングリコール0.5gをメスピペットにて採取
し、上記ビーカーに加えた。Comparative Example 3 Amine solution of hydroxyplatinic acid (Pt concentration: 20% by weight) I
g was collected with a measuring pipette and placed in a 2o-beaker. 0.5 g of ethylene glycol was collected with a measuring pipette and added to the beaker.
両者を筆で良く混合した後、30メツシユ、4cm角の
カンタル金網(1100°Cで3時間熱処理済み)に筆
で上記溶液を両面に隅無く塗り付けた。After mixing the two well with a brush, the above solution was applied to both sides of a 30-mesh, 4 cm square Kanthal wire mesh (heat-treated at 1100° C. for 3 hours) without any corners using a brush.
混合溶液を塗り付けたカンタル金網をマツフル炉内で7
00°C130分間焼成した。金網を秤量した結果、重
量はほとんど増えていなかった。The Kanthal wire mesh coated with the mixed solution was heated in a Matsufuru furnace.
It was baked at 00°C for 130 minutes. As a result of weighing the wire mesh, there was almost no increase in weight.
比較例4
水酸化白金酸のアミン溶液(Pt濃度;20重量%)1
.5gをメスピペットにて採取し、20++i2ビーカ
ーに入れた。30メツシユ、4cm角のカンタル金網(
1100°Cで3時間熱処理済み)に筆で上記溶液を両
面に隅無く塗り付けた後、マツフル炉内で700°C1
30分間焼成した。金網を秤量した結果、重量はほとん
ど増えていなかった。Comparative Example 4 Amine solution of hydroxyplatinic acid (Pt concentration: 20% by weight) 1
.. 5 g was collected with a graduated pipette and placed in a 20++i2 beaker. 30 mesh, 4cm square Kanthal wire mesh (
Heat-treated at 1100°C for 3 hours), apply the above solution to both sides with a brush without any corners, then heat at 700°C in a Matsufuru furnace.
It was baked for 30 minutes. As a result of weighing the wire mesh, there was almost no increase in weight.
重量測定
比較例3.4で得られた触媒はPt担持後に重量測定し
た結果、PLがほとんど付いていないことがわかった。Weight measurement The catalyst obtained in Comparative Example 3.4 was weighed after supporting Pt, and it was found that almost no PL was attached.
五ME独
実施例1〜lO及び比較例1で得られた触媒は、白金族
金属が数〜十数重量%も担持されているにもかかわらず
、叩いたり、刷毛で擦ったりしても、はとんど白金族金
属の剥離は生じなかった。一方、比較例2で得られた触
媒は叩いたり、擦ったりすると大半のPtが金網から剥
離してしまい、重量を測定するとほとんどptを担持す
る前の重量にまで戻ってしまった。Although the catalysts obtained in 5ME German Examples 1 to 1O and Comparative Example 1 supported platinum group metals in an amount of several to ten-odd percent by weight, they did not react well even when beaten or rubbed with a brush. Almost no peeling of the platinum group metal occurred. On the other hand, when the catalyst obtained in Comparative Example 2 was struck or rubbed, most of the Pt was peeled off from the wire gauze, and when the weight was measured, the weight returned to almost the same as before supporting Pt.
特開昭59−123535号公報に白金族金属の微粉末
及びそのイオンの共存を特徴とする白金族金属触媒の担
持方法が開示されているが、比較例2で得られた触媒の
剥離試験から明らかなように、同公報に開示された有機
バインダー(エチルセルロースのカルピトール水溶液)
では白金族金属の剥離を抑えることができないことがわ
かった。JP-A-59-123535 discloses a method for supporting a platinum group metal catalyst characterized by the coexistence of a fine powder of a platinum group metal and its ions, but from a peel test of the catalyst obtained in Comparative Example 2, As is clear, the organic binder (carpitol aqueous solution of ethyl cellulose) disclosed in the same publication
It was found that the peeling of platinum group metals could not be suppressed with this method.
それに対し、実施例1〜IOで得られた触媒の剥離試験
から明らかなように、本発明において開示された各種有
機物を用いれば、金属材料からの白金族金属の剥離はほ
とんど起こらないことがわかっlこ 。On the other hand, as is clear from the peeling tests of the catalysts obtained in Examples 1 to IO, when the various organic substances disclosed in the present invention are used, platinum group metals are hardly peeled off from metal materials. lko.
ヱヱJuす」服杢
実施例1〜10及び比較例1で得られた触媒をそれぞれ
20〜80倍の光学顕微鏡で観察した。The catalysts obtained in Examples 1 to 10 and Comparative Example 1 were each observed using an optical microscope with a magnification of 20 to 80 times.
実施例1.2.4〜10及び比較例1で得られた触媒は
カンタル線の表面にほぼ均一に白金族金属が分布してい
た。白金族金属の付着状態は、エチレングリコール系有
機物、プロピレングリコール系有機物を用いた実施例1
,2.4〜10で得られた触媒ではカンタル線の表面に
かなり粗く付いていたのに対し、電気メツキ法を用いた
比較例Iで得られた触媒ではカンタル線の表面に滑らか
に付いていた。また、同じポリエチレングリコールを用
いながらカンタル金網に前処理を施さなかった実施例3
で得られた触媒はPLがカンタル金網のコーナ一部にや
や濃く、直線部にやや薄く分布した。Ptの付着状態は
、実施例1,2.4〜lOで得られた触媒と同様にカン
タル線の表面にかなり粗く付いていた。In the catalysts obtained in Examples 1.2.4 to 10 and Comparative Example 1, the platinum group metal was almost uniformly distributed on the surface of the Canthal wire. The state of adhesion of the platinum group metal was as shown in Example 1 using an ethylene glycol-based organic substance and a propylene glycol-based organic substance.
The catalysts obtained in , 2.4 to 10 adhered to the surface of the Kanthal wire rather roughly, whereas the catalyst obtained in Comparative Example I using the electroplating method adhered smoothly to the surface of the Kanthal wire. Ta. In addition, Example 3 in which the same polyethylene glycol was used but the Kanthal wire mesh was not pretreated.
In the catalyst obtained in the above, PL was distributed slightly thickly in the corners of the Kanthal wire gauze and slightly thinly distributed in the straight parts. Similar to the catalysts obtained in Examples 1 and 2.4 to 1O, Pt was adhered quite roughly to the surface of the Kanthal wire.
実施例1,2.4〜IOで得られた触媒の光学顕微鏡観
察の結果を比較例Iで得られた触媒と比較すると、ジエ
チレングリコール、トリエチレングリコール、テトラエ
チレングリコール、ポリエチレングリコール、プロピレ
ングリコール、ジエチレングリコール、トリプロピレン
グリコールの少なくとも一つを用いれば、カンタル線の
表面に白金族金属がほぼ均一に、しがも、電気メツキ法
(比較例1)に比べてかなり粗く(有効表面積が多く)
担持されていることがわかった。Comparing the results of optical microscopic observation of the catalysts obtained in Examples 1 and 2.4 to IO with the catalyst obtained in Comparative Example I, it was found that diethylene glycol, triethylene glycol, tetraethylene glycol, polyethylene glycol, propylene glycol, diethylene glycol If at least one of tripropylene glycol is used, the platinum group metal can be almost uniformly coated on the surface of the Kanthal wire, but it is considerably rougher (larger effective surface area) than the electroplating method (Comparative Example 1).
It was found that it was carried.
さらに、実施例1〜3で得られた触媒の光学顕微鏡観察
から明らかなように、カンタル金網を予め、熱処理、化
学的もしくは物理的処理等を施すことにより金属表面を
あらしたほうが、白金族金属は表面により均一に分布す
ることがわかった。Furthermore, as is clear from the optical microscopic observation of the catalysts obtained in Examples 1 to 3, it is better to roughen the metal surface by subjecting the Kanthal wire gauze to heat treatment, chemical or physical treatment, etc. was found to be more uniformly distributed on the surface.
区血星見
ガスバーナーの炎で実施例1〜10及び比較例1で得ら
れた触媒を炙って赤熱させた後、息を勢いよく吹き付け
てガスバーナーの炎を消し、ガスバーナーのガスのみで
触媒燃焼するか(赤熱するか)否か試験した。実施例1
〜10及び比較例1で得られた触媒はいずれも最初は触
媒燃焼した。After roasting the catalysts obtained in Examples 1 to 10 and Comparative Example 1 with the flame of a gas burner, the catalysts obtained in Examples 1 to 10 and Comparative Example 1 were heated to red hot, and then the flame of the gas burner was extinguished by blowing forcefully with air, and the flame of the gas burner was extinguished using only the gas from the gas burner. A test was conducted to see if it would catalytically burn (become red hot). Example 1
The catalysts obtained in Comparative Example 1 and Comparative Example 1 all underwent catalytic combustion at first.
ただし、比較例1の電気メツキ処理した触媒のみが数回
の燃焼試験後ですでに赤熱せず、触媒活性を失った。こ
のような結果より、電気メツキ処理した白金族金属担持
金属触媒は触媒活性が著しく劣っていると言える。However, only the electroplated catalyst of Comparative Example 1 did not become red hot after several combustion tests and lost its catalytic activity. From these results, it can be said that the electroplated platinum group metal-supported metal catalyst has significantly inferior catalytic activity.
これに対し、実施例1〜10で得られた触媒はいずれも
触媒燃焼をし続け、特に、ptを担持した実施例1及び
実施例4〜8で得られた触媒は8000回もの吹き消し
試験後も触媒燃焼による赤熱の様子はまったく変化しな
かった。On the other hand, all the catalysts obtained in Examples 1 to 10 continued to perform catalytic combustion, and in particular, the catalysts obtained in Examples 1 and 4 to 8 carrying PT were subjected to 8000 blowout tests. Even after that, the appearance of red heat caused by catalytic combustion did not change at all.
属板への白金族金属の担
実施例11
実施例1と同じ方法で調製した混合溶液を4cm角のス
テンレス金属の薄板(1100°Cで3時間熱処理済み
)に筆で両面に隅無く付けた後、マツフル炉内で700
°0130分間焼成した。Ptの担持量は3重量%(2
0mg/ cm”)であった。Ptを担持したステンレ
ス金属を叩いたり、刷毛で擦ったりしてもほとんどPt
の剥離は生じなかった。Example 11 of loading platinum group metal onto a metal plate A mixed solution prepared in the same manner as in Example 1 was applied to a 4 cm square stainless metal thin plate (heat treated at 1100°C for 3 hours) on both sides without corners using a brush. After that, 700 in the Matsufuru furnace
Baked for 130 minutes. The amount of Pt supported was 3% by weight (2
0mg/cm"). Even if stainless metal carrying Pt is struck or rubbed with a brush, almost no Pt is removed.
No peeling occurred.
比較例5
比較例2と同じ方法で調製した混合溶液を4cm角のス
テンレス金属の薄板(1100°Cで3時間熱処理済み
)に筆で両面に隅無く塗り付けた後、マツフル炉内で7
00°C130分間焼成した。Comparative Example 5 A mixed solution prepared in the same manner as Comparative Example 2 was applied to a 4 cm square stainless metal thin plate (heat treated at 1100°C for 3 hours) on both sides with a brush, and then heated in a Matsufuru furnace for 7 hours.
It was baked at 00°C for 130 minutes.
PLを担持したステンレス金属を叩いたり、刷毛で擦っ
たりすると大半のPtが金属板から剥離してしまい、重
量を測定するとほとんどPtを担持する前の重量にまで
戻ってしまった。When the stainless steel metal supporting PL was struck or rubbed with a brush, most of the Pt was peeled off from the metal plate, and when the weight was measured, the weight returned to almost the same as before supporting Pt.
比較例5で得られた触媒の重量測定の結果より明らかな
ように、比較的白金族金属が剥離し難い金属板を担体と
して用いても、特開昭59−123535号公報に開示
されているエチルセルロースのカルピトール水溶液を有
機バインダーとして用いる限り、白金族金属の剥離を抑
えることはできなかった。As is clear from the results of the weight measurement of the catalyst obtained in Comparative Example 5, even if a metal plate from which the platinum group metal is relatively difficult to peel off is used as a carrier, the same method as disclosed in JP-A-59-123535 can be used. As long as an aqueous solution of ethyl cellulose in calpitol was used as an organic binder, it was not possible to suppress the peeling of platinum group metals.
[効果]
以上から明らかなように、本発明の方法により、金属材
料との密着性に優れ、触媒活性が高く、しかも、数〜十
数重量%もの白金族金属を一度で担持することのできる
白金族金属担持金属触媒を製造することができる。[Effects] As is clear from the above, the method of the present invention has excellent adhesion to metal materials, high catalytic activity, and can support several to tens of weight percent of platinum group metals at once. Platinum group metal supported metal catalysts can be produced.
Claims (1)
有する金属材料に白金族金属を担持した白金族金属担持
金属触媒の製造に際し、 (1)白金族金属の化合物 及び (2)下記式 ▲数式、化学式、表等があります▼ 式中、RはH又はCH_3を表わし、 RがHであるときは、n≧2であり、 RがCH_3であるときは、n≧1である、で表わされ
る化合物からなる群より選択した1種または2種以上の
化合物 を含有する溶液を金属材料に付着させた後、該金属材料
を熱処理することを特徴とする白金族金属担持金属触媒
の製造方法。[Scope of Claims] When producing a platinum group metal-supported metal catalyst in which a platinum group metal is supported on a metal material having a linear, net-like, plate-like, honeycomb-like, or ring-like shape, (1) platinum group metal Compound and (2) The following formula ▲ There are mathematical formulas, chemical formulas, tables, etc. ▼ In the formula, R represents H or CH_3, When R is H, n≧2, When R is CH_3, A platinum group metal, characterized in that a solution containing one or more compounds selected from the group consisting of compounds represented by n≧1 is applied to a metal material, and then the metal material is heat-treated. A method for producing a metal-supported metal catalyst.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8150389A JPH02261542A (en) | 1989-04-03 | 1989-04-03 | Production of metallic catalyst supporting platinum family metal |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8150389A JPH02261542A (en) | 1989-04-03 | 1989-04-03 | Production of metallic catalyst supporting platinum family metal |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH02261542A true JPH02261542A (en) | 1990-10-24 |
Family
ID=13748165
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8150389A Pending JPH02261542A (en) | 1989-04-03 | 1989-04-03 | Production of metallic catalyst supporting platinum family metal |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02261542A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6436873B1 (en) | 1998-06-19 | 2002-08-20 | Basf Aktiengesellschaft | Impregnating process for the application of active composition to structured supports or monoliths |
JP2006502860A (en) * | 2002-10-18 | 2006-01-26 | エミテック ゲゼルシヤフト フユア エミツシオンス テクノロギー ミツト ベシユレンクテル ハフツング | Catalyst support having passivation layer and method for producing the same |
-
1989
- 1989-04-03 JP JP8150389A patent/JPH02261542A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US6436873B1 (en) | 1998-06-19 | 2002-08-20 | Basf Aktiengesellschaft | Impregnating process for the application of active composition to structured supports or monoliths |
JP2006502860A (en) * | 2002-10-18 | 2006-01-26 | エミテック ゲゼルシヤフト フユア エミツシオンス テクノロギー ミツト ベシユレンクテル ハフツング | Catalyst support having passivation layer and method for producing the same |
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