JPH0813335B2 - Self-cleaning coating layer - Google Patents
Self-cleaning coating layerInfo
- Publication number
- JPH0813335B2 JPH0813335B2 JP63159978A JP15997888A JPH0813335B2 JP H0813335 B2 JPH0813335 B2 JP H0813335B2 JP 63159978 A JP63159978 A JP 63159978A JP 15997888 A JP15997888 A JP 15997888A JP H0813335 B2 JPH0813335 B2 JP H0813335B2
- Authority
- JP
- Japan
- Prior art keywords
- coating layer
- catalyst
- oil
- self
- oxide
- 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 - Fee Related
Links
- 239000011247 coating layer Substances 0.000 title claims description 29
- 238000004140 cleaning Methods 0.000 title claims description 6
- 229910052748 manganese Inorganic materials 0.000 claims description 12
- 238000007750 plasma spraying Methods 0.000 claims description 11
- 239000000758 substrate Substances 0.000 claims description 8
- 238000000034 method Methods 0.000 claims description 7
- 239000003054 catalyst Substances 0.000 description 29
- 240000008415 Lactuca sativa Species 0.000 description 9
- 230000003197 catalytic effect Effects 0.000 description 9
- 239000000463 material Substances 0.000 description 9
- 235000012045 salad Nutrition 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- 229910017566 Cu-Mn Inorganic materials 0.000 description 7
- 229910017871 Cu—Mn Inorganic materials 0.000 description 7
- 238000007254 oxidation reaction Methods 0.000 description 7
- 230000001965 increasing effect Effects 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 239000001301 oxygen Substances 0.000 description 5
- 239000007921 spray Substances 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 4
- 229910052802 copper Inorganic materials 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 239000000843 powder Substances 0.000 description 4
- UFTFJSFQGQCHQW-UHFFFAOYSA-N triformin Chemical compound O=COCC(OC=O)COC=O UFTFJSFQGQCHQW-UHFFFAOYSA-N 0.000 description 4
- 239000011230 binding agent Substances 0.000 description 3
- 210000003298 dental enamel Anatomy 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 3
- 229910044991 metal oxide Inorganic materials 0.000 description 3
- 150000004706 metal oxides Chemical class 0.000 description 3
- 238000006864 oxidative decomposition reaction Methods 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 230000010718 Oxidation Activity Effects 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 239000011248 coating agent Substances 0.000 description 2
- 238000000576 coating method Methods 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000000354 decomposition reaction Methods 0.000 description 2
- -1 enamel Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 229910052742 iron Inorganic materials 0.000 description 2
- 239000003973 paint Substances 0.000 description 2
- 238000007751 thermal spraying Methods 0.000 description 2
- 229910052723 transition metal Inorganic materials 0.000 description 2
- 150000003624 transition metals Chemical class 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 125000003178 carboxy group Chemical group [H]OC(*)=O 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000013329 compounding Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000010411 cooking Methods 0.000 description 1
- 230000007797 corrosion Effects 0.000 description 1
- 238000005260 corrosion Methods 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 239000010794 food waste Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 238000009413 insulation Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052759 nickel Inorganic materials 0.000 description 1
- 150000002823 nitrates Chemical class 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000002344 surface layer Substances 0.000 description 1
- 230000002195 synergetic effect Effects 0.000 description 1
- 229910000314 transition metal oxide Inorganic materials 0.000 description 1
Landscapes
- Catalysts (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は炭化水素系化合物の酸化触媒作用を有する被
覆層に関するものである。TECHNICAL FIELD The present invention relates to a coating layer having an oxidation catalyst action for hydrocarbon compounds.
従来の技術 従来より炭化水素系の酸化分解触媒としては、貴金属
や遷移金属の酸化物などが使用されてきている。例えば
炭化水素系化合物として、特に調理器の油汚れにみられ
るカルボキシル基を含む高級脂肪酸のトリグリセリドを
考えた場合、Mn,Cu,Fe,Co,Ni等の各金属酸化物かもしく
は各金属酸化物の混合物が酸化分解触媒として知られて
おり、調理器庫内壁面にこれらの酸化物などを主成分と
した触媒物質をホーローやガラス質の皮膜中に添加した
触媒コーティングがある。これらは無機質のバインダー
中に触媒を分散させたものを庫内壁面に塗布して被覆層
を形成し、油分や食品残査などを触媒的に高温下で分解
しようとするものであるが、触媒物質がホーローやガラ
ス質、塗料などの皮膜中に覆われて表面の露出が小なく
なるため450℃以上の高温が必要となり、更に低温で触
媒活性を有する被覆層が望まれている。BACKGROUND ART Conventionally, oxides of noble metals and transition metals have been used as hydrocarbon-based oxidative decomposition catalysts. For example, when considering a triglyceride of a higher fatty acid containing a carboxyl group found in oil stains of cookers as a hydrocarbon compound, each metal oxide such as Mn, Cu, Fe, Co, Ni or each metal oxide is considered. Is known as an oxidative decomposition catalyst, and there is a catalyst coating in which a catalyst material containing these oxides as a main component is added to a enamel or glassy film on the inner wall surface of the cooking chamber. These are those in which a catalyst is dispersed in an inorganic binder and applied to the inner wall surface to form a coating layer, which is intended to catalytically decompose oil and food residues at high temperatures. Since the substance is covered with a coating such as enamel, glass, or paint and the surface is not exposed, a high temperature of 450 ° C. or higher is required, and a coating layer having a catalytic activity at a lower temperature is desired.
発明が解決しようとする課題 上記従来技術においては、例えばトリグリセリドの酸
化分解反応に対して各金属酸化物の触媒活性が低いこ
と、また皮膜として用いる場合には触媒を耐熱性のバイ
ンダー中に分散させるために触媒表面の露出がなくなり
活性が低下することが問題である。また触媒表面の露出
を多くするためには被覆層をできるだけ多孔質にしなけ
ればならないが、反面多孔質にすることにより基材との
密着性や被覆層の耐蝕性、摩耗性が低下するという問題
があった。これらの問題が主要因となり実用化しにくい
などの2次的な問題が発生する。DISCLOSURE OF THE INVENTION Problems to be Solved by the Invention In the above conventional technique, for example, the catalytic activity of each metal oxide is low with respect to the oxidative decomposition reaction of triglyceride, and when used as a film, the catalyst is dispersed in a heat-resistant binder. Therefore, the problem is that the catalyst surface is not exposed and the activity is reduced. Also, in order to increase the exposure of the catalyst surface, the coating layer must be made as porous as possible, but on the other hand, making it porous reduces the adhesion to the substrate and the corrosion resistance and wear resistance of the coating layer. was there. These problems are the main factors, and secondary problems such as difficulty in practical use occur.
本発明は上記問題点を解決しようとするもので、触媒
自身、および触媒を基材上に被覆層として形成した場合
にも活性を高めることにより反応温度を低下させるセル
フクリーニング用被覆層を提供するものである。The present invention is intended to solve the above problems and provides a self-cleaning coating layer which lowers the reaction temperature by enhancing the activity of the catalyst itself and also when the catalyst is formed as a coating layer on a substrate. It is a thing.
課題を解決するための手段 上記問題点を解決するために本発明は、プラズマ溶射
により、耐熱性基材表面に希土類元素のCeと遷移金属の
Cu,Mnの複合酸化物の被覆層を、被覆層の膜厚方向にCe,
Cu,Mnの濃度勾配を持たせて形成するものであり、この
被覆層表面上で調理物から飛散する油分を分解しようと
するものである。Means for Solving the Problems In order to solve the above problems, the present invention, by plasma spraying, a rare earth element Ce and a transition metal on the surface of the heat resistant substrate.
Cu, Mn complex oxide coating layer, Ce, in the thickness direction of the coating layer
It is formed with a concentration gradient of Cu and Mn, and it is intended to decompose the oil content scattered from the food on the surface of the coating layer.
作用 上記構成による触媒被覆層の作用について説明する。
まず本発明の触媒であるCeACuBMnCOD(但しA=1,B+C
=1,0<B<1,0<C<1,D>0)で表わされる複合酸化
物は従来にない化合物であり、各成分の単一酸化物に比
べトリグリセリドの酸化に対して高い活性を示す。例え
ばCeO2,CuO,Cu2O,Mn2O3,MnO2のいずれに比べても酸化活
性が高い。これはCeとCu,Mnの3元素系酸化物において
は、酸化物の表面における元素が多くの原子価をとるか
らであり(例えばMnは3価、4価、Cuは1価、2価な
ど)、つまり単一成分では見られない異元素間での原子
価制御が行なわれ、反応に関してより適した表面を作る
からである。このことはXPSで認められる。Action The action of the catalyst coating layer having the above configuration will be described.
First, the catalyst of the present invention is Ce A Cu B Mn C O D (where A = 1, B + C
= 1,0 <B <1,0 <C <1, D> 0) is a compound oxide that has never existed before and has a higher activity for the oxidation of triglyceride than the single oxide of each component. Indicates. For example, the oxidation activity is higher than any of CeO 2 , CuO, Cu 2 O, Mn 2 O 3 , and MnO 2 . This is because in the three-element system oxide of Ce, Cu, and Mn, the element on the surface of the oxide takes many valences (for example, Mn is trivalent and tetravalent, Cu is monovalent and divalent, etc.). ), That is, valence control between different elements that is not found in a single component is performed, and a surface more suitable for reaction is created. This is confirmed by XPS.
本発明では上記した触媒を用いてプラズマ溶射により
触媒の単独膜を形成している。皮膜そのものが触媒であ
るためホーロー、ガラス質や塗料のようにフリットやバ
インダーで触媒が覆われ固められたものではない。従っ
て本発明の被覆層は触媒と油分との直接接触、反応界面
への酸素の供給が十分に行なわれ触媒性能を向上させる
ことができる。更に被覆層の膜厚方向にCe,Cu,Mnの濃度
勾配を有することが可能なため、例えば被覆層の耐熱性
基材表面側にCeの含有率を高くすることにより耐熱性基
材の表面積を大きくし、被覆層の表面側にCu,Mnの含有
率を高くすることにより、より酸化活性の高い被覆層を
形成することができるのである。In the present invention, a single film of the catalyst is formed by plasma spraying using the above-mentioned catalyst. Since the film itself is a catalyst, it is not hardened by covering the catalyst with frit or binder like enamel, glass or paint. Therefore, in the coating layer of the present invention, the direct contact between the catalyst and the oil and the supply of oxygen to the reaction interface are sufficiently carried out to improve the catalytic performance. Furthermore, since it is possible to have a concentration gradient of Ce, Cu, Mn in the thickness direction of the coating layer, for example, by increasing the Ce content on the surface side of the heat-resistant substrate of the coating layer, the surface area of the heat-resistant substrate is increased. By increasing the content of Cu and Mn on the surface side of the coating layer, a coating layer having higher oxidation activity can be formed.
実施例 以下、本発明の一実施例について説明する。まず触媒
の作成法について説明する。Example Hereinafter, an example of the present invention will be described. First, a method for preparing the catalyst will be described.
Ce,Cu,Mnの硝酸塩を所定のモル比になるようにした水
溶液を作り共沈法により沈殿物を得たのち熱分解してCe
ACuBMuCOD(但しA=1,B+C=1,0<B<1,0<C<1,D
>0)で表わされる複合酸化物とした。比較のために単
一および二種成分の遷移金属酸化物の沈殿法により作成
した。Ce, Cu, and Mn nitrates were made into an aqueous solution with a predetermined molar ratio, and a precipitate was obtained by the coprecipitation method.
A Cu B Mu C O D (However, A = 1, B + C = 1,0 <B <1,0 <C <1, D
The composite oxide represented by> 0). For comparison, single and binary transition metal oxides were prepared by the precipitation method.
上記した方法で作成した触媒粉末を用い、ブラスト処
理を施したステンレス基板(板厚1mm)上にプラズマス
プレーを行い、膜厚20μmで触媒の溶射皮膜を形成し
た。Using the catalyst powder prepared by the above method, plasma spraying was performed on a blasted stainless steel substrate (plate thickness 1 mm) to form a catalyst spray coating with a film thickness of 20 μm.
なお、プラズマ溶射は永田鉄工(株)製のNT30型直流
プラズマスプレー装置を使用した。For plasma spraying, an NT30 type DC plasma spray device manufactured by Nagata Iron Works Co., Ltd. was used.
これを試験片として370℃での油分の浄化能力を確認
した。一定量のサラダ油を試験片上に滴下し、370℃の
オーブン中に保持してサラダ油の変化を見たものであ
る。結果を第1表に示す。Using this as a test piece, the ability to purify oil at 370 ° C was confirmed. A certain amount of salad oil was dropped on the test piece and kept in an oven at 370 ° C. to see the change in salad oil. The results are shown in Table 1.
以上の結果から、Ce−Cu−Mn複合酸化物をプラズマ溶
射した被覆層は、トリグリセリドの酸化反応に対する促
進効果が極めて大きいことがわかる。 From the above results, it can be seen that the coating layer obtained by plasma spraying the Ce-Cu-Mn composite oxide has an extremely large promoting effect on the oxidation reaction of triglyceride.
触媒粉末にサラダ油を1μ程度滴下して加熱を行
い、サラダ油の燃焼が開始する温度を確認した。Ce−Cu
−Mn系においては約240〜250℃で燃焼の開始が認められ
た。About 1 μ of salad oil was dropped on the catalyst powder and heated to confirm the temperature at which the combustion of the salad oil started. Ce-Cu
In the -Mn system, the onset of combustion was observed at about 240-250 ℃.
Mn酸化物やCu酸化物では300℃でもこのような現象は
おこらず触媒活性の違いが明確でありCe−Cu−Mn系が特
に油の分解に適していることがわかる。これは複合酸化
物であるため複合効果による酸化反応の促進作用、Ce
の、特にバルクにおけるMnなどへの酸素の供給源として
の働き等により、このように油分の分解に対する高い活
性が発揮されているものと思われる。With Mn oxides and Cu oxides, such a phenomenon does not occur even at 300 ° C, and the difference in catalytic activity is clear, indicating that the Ce-Cu-Mn system is particularly suitable for oil decomposition. Since this is a complex oxide, it accelerates the oxidation reaction due to the complex effect, Ce
It is considered that the high activity for the decomposition of oil is exerted as described above, due to its function as a source of oxygen for Mn and the like particularly in the bulk.
更に、Ce−Cu−Mn系の複合酸化物における各元素の機
能を考えてみると、Ce酸化物は第2表に示したように、
単一酸化物としての表面積も大きく、またCu−Mn系の複
合酸化物と組み合わせることにより更に大きな表面積の
触媒を作っていることがわかる。Ce酸化物がバルク中で
Mnなどへの酸素の供給源になっていることは既に上記し
た通りである。Furthermore, considering the function of each element in the Ce-Cu-Mn-based composite oxide, as shown in Table 2, the Ce oxide is
It can be seen that the surface area as a single oxide is also large, and that a catalyst with a larger surface area is made by combining with a Cu-Mn-based composite oxide. Ce oxide in bulk
As described above, it is a source of oxygen supply to Mn and the like.
次に同じく沈殿法により作成したCeOX,MnOX,CuOX(X:
未決定)について各粉末とサラダ油を一定の重量比で混
合し、熱天秤を用い昇温によるサラダ油の重量変化を追
った。第3図にその結果を示す。第3図よりサラダ油の
酸化に対してはCeOXよりもMnOXやCuOXの方が触媒活性が
高いことがわかる。Ce−Cu−Mn系の複合酸化物では、複
合することにより更に相乗的な効果もおこり従来にない
高活性を示しているのである。 Next, CeO X , MnO X , CuO X (X:
(Undetermined), each powder and salad oil were mixed at a constant weight ratio, and the weight change of the salad oil due to the temperature rise was followed using a thermobalance. The results are shown in FIG. From Figure 3, it can be seen that MnO X and CuO X have higher catalytic activity than CeO X for the oxidation of salad oil. In the case of Ce-Cu-Mn-based complex oxides, the compounding of them causes a synergistic effect, and shows a high activity that has never been seen before.
そこで以上の結果をふまえ、更にプラズマ溶射の利点
を活かし更に高活性な被覆層を形成する試みを行った。
プラズマ溶射では2種類以上の粉末を別々の溶射口から
同時に同じ基材上に溶射して皮膜を形成することができ
る。そこで第1図に示したように、CeOXとCu−MnOXを別
々の溶射口2,3から耐熱性基材1に溶射して被覆層4を
形成した。その際第2図に示したようにそれぞれの溶射
量を経時的に変化させ、T時間後に溶射をストップさ
せ、被覆層の厚み方向にCe,Cu,Mnの濃度勾配を持たせ
た。Ce,Cu,Mnの濃度勾配を持たせて形成した被覆層4の
上にサラダ油を滴下し温度を上げると、350℃で約20分
後に油は完全に分解し残渣は残らなかった。濃度勾配を
持たせずに形成した被覆層では、第1表に示したように
370℃で約30〜35分で油は分解している。このことは基
材側にCeOXを多くすることでより表面積の大きな触媒層
を形成し、また触媒活性の高いCu−Mnを表面層に多くす
ることで総合的に、油の酸化に対して高い触媒活性を示
しているためと思われる。Therefore, based on the above results, an attempt was made to form a coating layer having higher activity by taking advantage of plasma spraying.
In plasma spraying, two or more kinds of powders can be simultaneously sprayed from different spray ports onto the same base material to form a film. Therefore, as shown in FIG. 1, CeO X and Cu—MnO X were sprayed onto the heat-resistant substrate 1 from separate spray ports 2 and 3 to form a coating layer 4. At that time, as shown in FIG. 2, the respective thermal spraying amounts were changed with time, the thermal spraying was stopped after T time, and a Ce, Cu, Mn concentration gradient was provided in the thickness direction of the coating layer. When salad oil was dropped on the coating layer 4 formed with a concentration gradient of Ce, Cu, Mn and the temperature was raised, the oil completely decomposed after about 20 minutes at 350 ° C. and no residue remained. In the coating layer formed without the concentration gradient, as shown in Table 1,
The oil decomposes in about 30 to 35 minutes at 370 ° C. This means that by increasing CeO X on the base material side, a catalyst layer with a larger surface area is formed, and by increasing Cu-Mn, which has high catalytic activity, in the surface layer, it is possible to prevent oxidation of oil overall. This is probably because it exhibits high catalytic activity.
発明の効果 以上説明の通り、本発明によればプラズマ溶射により
基材表面に触媒活性が極めて高いCe−Cu−Mn系複合酸化
物の触媒を用い触媒単独のセルフクリーニング被覆層を
形成したものであるため触媒と油分との接触面積が大き
く、プラズマ溶射皮膜は好適な多孔度を有するポーラス
な皮膜であるため触媒と油分との反応界面に酸素が十分
に供給される。従って酸化反応で消費される酸素も、皮
膜の内部及び空気中から補給されるため性能低下もなく
長期間触媒活性を保持することができる。また膜厚方向
に自由にCe,Cu,Mnの濃度勾配を有することができるた
め、より高活性な皮膜を形成することができる。またCe
OXは基材との密着性がよく、酸に対して強いため、被覆
層の基材側にCeOXの含有率を高くしておくことにより基
材との密着性が向上し、また酸に触れることがあっても
基材が酸で腐食することが防止できるのである。As described above, according to the present invention, the self-cleaning coating layer of the catalyst alone is formed on the surface of the base material by the plasma spraying using the catalyst of the extremely high catalytic activity Ce-Cu-Mn composite oxide. Therefore, the contact area between the catalyst and oil is large, and since the plasma spray coating is a porous film having a suitable porosity, oxygen is sufficiently supplied to the reaction interface between the catalyst and oil. Therefore, the oxygen consumed in the oxidation reaction is also replenished from the inside of the film and from the air, so that the catalytic activity can be maintained for a long period of time without deterioration in performance. Further, since a Ce, Cu, Mn concentration gradient can be freely provided in the film thickness direction, a more highly active film can be formed. Also Ce
O X has good adhesion to the base material and is strong against acid. Therefore, increasing the CeO X content on the base material side of the coating layer improves the adhesion to the base material, and It is possible to prevent the base material from being corroded by acid even if it is touched.
本発明のセフルクリーニング被覆層をオーブン等の庫
内壁面に適用することにより、従来の焼切り方式のオー
ブンで熱セルフクリーニングする場合500〜550℃の温度
に保持する必要があったがこれを400℃以下に下げるこ
とが可能となり省エネや断熱の面で多大な効果を有する
ものである。また油汚れを完全に分解することができる
のでオーブン庫内を長く新品同様の状態に保つことがで
きる。When the self-cleaning coating layer of the present invention is applied to the inner wall surface of an oven or the like, it is necessary to maintain the temperature at 500 to 550 ° C. in the case of thermal self-cleaning in a conventional oven of the burning-off method. It is possible to reduce the temperature to below ℃, which has a great effect on energy saving and heat insulation. In addition, since oil stains can be completely decomposed, the inside of the oven can be kept in a state like a new one for a long time.
第1図は本発明の一実施例による被覆層の断面概念図、
第2図はプラズマ溶射における溶射量制御方法の一例を
示す相関グラフ、第3図は各種酸化物とサラダ油を混合
したものの熱重量変化曲線である。 1……耐熱性基材、2,3……プラズマ溶射口、4……プ
ラズマ溶射触媒皮膜。FIG. 1 is a schematic sectional view of a coating layer according to an embodiment of the present invention,
FIG. 2 is a correlation graph showing an example of a spraying amount control method in plasma spraying, and FIG. 3 is a thermogravimetric change curve of a mixture of various oxides and salad oil. 1 ... Heat resistant base material, 2, 3 ... Plasma spray port, 4 ... Plasma spray catalyst film.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 磯谷 守 大阪府門真市大字門真1006番地 松下電器 産業株式会社内 (56)参考文献 特開 平1−304049(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Mamoru Isoya 1006 Kadoma, Kadoma City, Osaka Prefecture Matsushita Electric Industrial Co., Ltd. (56) References JP-A-1-304049 (JP, A)
Claims (1)
Mnから成る複合酸化物の被覆層であり、前記複合酸化物
はCeACeBMnCOD(但しA=1,B+C=1,O<B<1,O<C<
1,D>0)で表わされる組成を有し、更に前記被覆層は
膜厚方向にCe,Cu,Mnの濃度勾配を有することを特徴とす
るプラズマ溶射法によって形成されたセルフクリーニン
グ用被覆層。1. Ce, Cu, formed on a substrate by plasma spraying,
A coating layer of a complex oxide composed of Mn, wherein the complex oxide is Ce A Ce B Mn C O D (where A = 1, B + C = 1, O <B <1, O <C <
1, D> 0), and the coating layer has a concentration gradient of Ce, Cu, Mn in the thickness direction, and is formed by a plasma spraying method for self-cleaning. .
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63159978A JPH0813335B2 (en) | 1988-06-28 | 1988-06-28 | Self-cleaning coating layer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP63159978A JPH0813335B2 (en) | 1988-06-28 | 1988-06-28 | Self-cleaning coating layer |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH029451A JPH029451A (en) | 1990-01-12 |
| JPH0813335B2 true JPH0813335B2 (en) | 1996-02-14 |
Family
ID=15705330
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP63159978A Expired - Fee Related JPH0813335B2 (en) | 1988-06-28 | 1988-06-28 | Self-cleaning coating layer |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0813335B2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5204302A (en) * | 1991-09-05 | 1993-04-20 | Technalum Research, Inc. | Catalyst composition and a method for its preparation |
-
1988
- 1988-06-28 JP JP63159978A patent/JPH0813335B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH029451A (en) | 1990-01-12 |
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