JPH05138044A - Productiohn of lils and fats decomposing film - Google Patents

Productiohn of lils and fats decomposing film

Info

Publication number
JPH05138044A
JPH05138044A JP30301291A JP30301291A JPH05138044A JP H05138044 A JPH05138044 A JP H05138044A JP 30301291 A JP30301291 A JP 30301291A JP 30301291 A JP30301291 A JP 30301291A JP H05138044 A JPH05138044 A JP H05138044A
Authority
JP
Japan
Prior art keywords
fats
film
decomposing
oils
coating material
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP30301291A
Other languages
Japanese (ja)
Inventor
Akio Fukuda
明雄 福田
Noriyuki Komeno
範幸 米野
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.)
Panasonic Holdings Corp
Original Assignee
Matsushita Electric Industrial 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 Matsushita Electric Industrial Co Ltd filed Critical Matsushita Electric Industrial Co Ltd
Priority to JP30301291A priority Critical patent/JPH05138044A/en
Publication of JPH05138044A publication Critical patent/JPH05138044A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To produce an oils and fats decomposing film decomposing and purifying the oil contamination of a cooking apparatus at low temp. within a short time. CONSTITUTION:Coating material containing oxide of either one of manganese, iron, cobalt and copper or composite oxide of them as an oils and fats decomposing catalyst and containing metal phosphate or metal silicate as a binder is prepared and applied to the surface of a heated base material and cured to obtain an oils and fats decomposing film.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、調理器などの油汚れの
浄化を行なう油脂類分解被膜の製造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a film for decomposing oils and fats for purifying oil stains on cookers and the like.

【0002】[0002]

【従来の技術】従来の製造方法は図6に示すように、触
媒とバインダーを含有する塗料を調合し、調合した塗料
を基材の表面に塗布し、その後加熱して塗料を硬化して
いた。そして塗料の硬化方法は図7に示すように、塗料
の塗布された基材を焼付炉に入れて順次温度を上げ
(A)、一定温度に保持(B)して硬化した後、次第に
温度を下げていた(C)。
2. Description of the Related Art In a conventional manufacturing method, as shown in FIG. 6, a paint containing a catalyst and a binder is prepared, the prepared paint is applied to the surface of a substrate, and then the paint is cured by heating. .. Then, as shown in FIG. 7, the method for curing the paint is as follows. The base material coated with the paint is put into a baking oven and the temperature is sequentially raised (A) and kept at a constant temperature (B) to cure, and then the temperature is gradually increased. It was lowered (C).

【0003】[0003]

【発明が解決しようとする課題】しかしながら、上記従
来の方法で製造した膜厚約100μmの被膜上にサラダ
油を滴下して電気オーブン中にて分解浄化テストを行な
うと、400℃では数時間をかけないと完全に分解しな
い。これはバインダーがホーローフリットであっても、
触媒が代っても同じことである。400℃よりも低温、
短時間では酸化反応が十分に進まず、タール状の残渣が
残ってしまう。
However, when salad oil was dropped on the coating film having a thickness of about 100 μm produced by the conventional method and a decomposition and purification test was conducted in an electric oven, it took several hours at 400 ° C. Without it, it will not be completely decomposed. Even if the binder is a hollow frit,
It is the same even if the catalyst is replaced. Lower than 400 ° C,
In a short time, the oxidation reaction does not proceed sufficiently and a tar-like residue remains.

【0004】このようになる原因はいくつかあるが、第
1は反応に必要な酸素の供給が少ないこと、第2は触媒
表面がバインダーにより覆われてしまい触媒表面積が見
かけ上小さくなっていることなどによると考えられる。
There are several causes for this, the first is that the supply of oxygen necessary for the reaction is small, and the second is that the surface of the catalyst is covered with the binder and the surface area of the catalyst is apparently small. Etc.

【0005】本発明は、このような従来の問題を解消
し、低温において短時間で油汚れを分解浄化する油脂類
分解被膜の製造方法を提供することを目的としている。
It is an object of the present invention to solve the above-mentioned conventional problems and to provide a method for producing a decomposed film of oils and fats which decomposes and purifies oil stains at a low temperature in a short time.

【0006】[0006]

【課題を解決するための手段】上記の目的を達成するた
めに本発明の油脂類分解被膜の製造方法は、油脂類分解
触媒として、マンガン,鉄,コバルトおよび銅の群から
選択された一種以上の酸化物または複合酸化物を含有
し、バインダーとして、金属リン酸塩または金属ケイ酸
塩を含有する塗料を調合し、前記塗料を加熱した基材の
表面に塗布し、硬化する。
In order to achieve the above object, the method for producing a film for decomposing oils and fats according to the present invention comprises, as a catalyst for decomposing oils and fats, one or more selected from the group consisting of manganese, iron, cobalt and copper. A paint containing the oxide or complex oxide of 1) and a metal phosphate or a metal silicate as a binder is prepared, and the paint is applied to the surface of a heated substrate and cured.

【0007】[0007]

【作用】本発明は、上記した構成によって、基材が加熱
された状態で塗料が塗布されるので、塗料の溶媒である
水の突沸により孔径と多孔度が大きく、表面の形状も凹
凸に富む被膜が製造され、酸化反応に必要な酸素が多量
に供給されることになる。
According to the present invention, since the coating material is applied while the base material is heated by the above-mentioned constitution, the pore diameter and the porosity are large due to the bumping of water which is the solvent of the coating material, and the surface shape is also uneven. A film is produced and a large amount of oxygen necessary for the oxidation reaction is supplied.

【0008】[0008]

【実施例】以下本発明の一実施例について図面を参照し
ながら説明する。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described below with reference to the drawings.

【0009】図1は本実施例の製造方法の工程図であ
る。同図に示すように、まず、塗料を調合する。本実施
例ではバインダーとして金属リン酸塩〔朝日化学工業
(株)製のスミセラムP−450〕を用い、油脂類分解
触媒としてマンガン,鉄,銅からなる複合酸化物(Fe
2 3 ・Mn2 3 ・CuO)を用いて両者を混合して
塗料を調合した。その後、ステンレス板(SUS43
0、寸法:0.5t×100w×100lmm)からなる基
材を電気オーブン中で200℃に加熱し、取り出してす
ぐに塗料を塗布した。その後300℃に加熱された電気
オーブン中で30分硬化した後冷却して油脂類分解被膜
を製造した。本実施例の加熱、硬化方法は図2に示すよ
うになり、図7に示した従来の方法と相違する点は、塗
料の塗布された基材を焼付炉に入れて順次温度を上げる
工程Aがない点である。
FIG. 1 is a process diagram of the manufacturing method of this embodiment. As shown in the figure, first, a paint is prepared. In this example, a metal phosphate [Sumiceram P-450 manufactured by Asahi Kagaku Kogyo Co., Ltd.] was used as a binder, and a composite oxide (Fe containing manganese, iron, copper was used as a fat and oil decomposition catalyst.
2 O 3 .Mn 2 O 3 .CuO) was mixed to prepare a coating material. After that, stainless steel plate (SUS43
A substrate consisting of 0, dimensions: 0.5 t × 100 w × 100 lmm) was heated to 200 ° C. in an electric oven, taken out, and the coating was applied immediately. Then, it was cured in an electric oven heated to 300 ° C. for 30 minutes and then cooled to produce a fat and oil decomposition film. The heating and curing method of this embodiment is as shown in FIG. 2, and is different from the conventional method shown in FIG. 7 in that the base material coated with the coating material is placed in a baking oven and the temperature is sequentially raised. There is no point.

【0010】本実施例の製造方法によれば、塗料が基材
に付着した瞬間から水の蒸発が始まり孔径と多孔度が大
きく、表面の形状も凹凸に富む被膜となる。孔径は数1
0μm〜数100μmの幅広い分布の被膜が得られる。
基材温度は被膜の性状を決める重要な要因であり、20
0〜500℃が望ましい。200℃未満では孔径、多孔
度および表面の凹凸があまり大きくならず、500℃を
越えると塗料が基材表面を濡らすことが困難になり好ま
しくない。
According to the manufacturing method of this embodiment, evaporation of water starts from the moment when the coating material adheres to the substrate, the pore size and the porosity are large, and the surface shape is a film having a lot of irregularities. Pore size is a few
A film having a wide distribution of 0 μm to several 100 μm can be obtained.
The base material temperature is an important factor that determines the properties of the coating film.
0-500 degreeC is desirable. If it is less than 200 ° C, the pore size, porosity and surface irregularities do not become so large, and if it exceeds 500 ° C, it becomes difficult for the paint to wet the surface of the substrate, which is not preferable.

【0011】また、本実施例の製造方法によれば、基材
温度が高いため塗布回数1回あたりの付着量を多くする
ことができ、従来の製造方法より膜厚の大きい被膜を短
時間で製造できる。油脂類分解被膜としては膜厚が大き
いほど浄化の処理量が増すことになる。本実施例により
製造した油脂類分解被膜の断面は図3に示すように、ス
テンレスからなる基材1の表面に、複合酸化物(Fe2
3 ・Mn2 3 ・CuO)からなる触媒2,金属リン
酸塩からなるバインダー3,閉孔4と開孔5からなる被
膜が形成されている。
Further, according to the manufacturing method of the present embodiment, since the substrate temperature is high, it is possible to increase the amount of adhesion per application number of times, and it is possible to form a coating having a larger film thickness in a shorter time than the conventional manufacturing method. Can be manufactured. As the oil and fat decomposition film has a larger film thickness, the amount of purification treatment increases. As shown in FIG. 3, the cross-section of the oil and fat decomposition film produced by this example shows a complex oxide (Fe 2
O 3 · Mn 2 O 3 · CuO) as a catalyst, a metal phosphate as a binder 3, a closed hole 4 and an opening 5 as a coating film.

【0012】本実施例の製造方法によれば、従来の製造
方法より開孔5の割合を多くすることができる。
According to the manufacturing method of this embodiment, the ratio of the openings 5 can be increased as compared with the conventional manufacturing method.

【0013】次に本実施例と従来例のサラダ油の浄化率
を比較した。浄化率は、被膜上にサラダ油をスポイドで
1滴あたり約25mgを5滴滴下した後、大気中で10
℃/分で昇温しながら重量変化を測定して浄化率を求め
た。その結果を図4に示す。同図より明らかなように、
従来例ではサラダ油を完全に分解するためには500℃
近くまで温度を高くする必要があったが、本実施例では
330℃でよい。
Next, the purification rates of the salad oils of this example and the conventional example were compared. The purification rate was 10 in the atmosphere after dropping 5 drops of salad oil on the film with a drop of about 25 mg per drop.
The weight change was measured while raising the temperature at ° C / min to obtain the purification rate. The result is shown in FIG. As is clear from the figure,
In the conventional example, 500 ℃ to completely decompose the salad oil.
Although it was necessary to raise the temperature to near, 330 ° C. is sufficient in this embodiment.

【0014】また、サラダ油100mgの吸収時間を比
較すると(表1)のようになり、本実施例による被膜は
多孔度が大きいため吸収時間が極めて短い。このため浄
化の処理量が増すことになる。
A comparison of the absorption time of 100 mg of salad oil is as shown in Table 1, and the film according to this example has a large porosity, and therefore the absorption time is extremely short. Therefore, the amount of purification treatment increases.

【0015】[0015]

【表1】 [Table 1]

【0016】図5は本実施例による被膜にサラダ油を滴
下し、300℃において種々の酸素濃度での重量残率の
経時変化を測定した結果であり、酸素濃度が高いほど短
時間で重量残率が低くなる。このことより油脂類分解被
膜では多孔度を大きくして酸素濃度を高くするほど浄化
能が高くなると考えられる。
FIG. 5 shows the results of measuring the time-dependent change in the weight residual ratio at various oxygen concentrations at 300 ° C. by dropping salad oil on the coating film according to this example. The higher the oxygen concentration, the shorter the weight residual ratio. Will be lower. From this, it is considered that in the oil and fat decomposition film, the purifying ability becomes higher as the porosity is increased and the oxygen concentration is increased.

【0017】なお、実施例においては、バインダーとし
て金属リン酸塩について説明したがこれに代えて金属ケ
イ酸塩を用いても同様の効果が得られる。
In the examples, the metal phosphate was explained as the binder, but the same effect can be obtained by using a metal silicate instead.

【0018】また、触媒としては実施例のマンガン,
鉄,銅の複合酸化物(Fe2 3 ・Mn2 3 ・Cu
O)に代えて、マンガン,鉄,コバルトおよび銅の群か
ら選択された一種以上の酸化物または複合酸化物を用い
ても同様の効果が得られる。
As the catalyst, manganese of the embodiment,
Complex oxide of iron and copper (Fe 2 O 3 · Mn 2 O 3 · Cu
The same effect can be obtained by using one or more oxides or composite oxides selected from the group of manganese, iron, cobalt and copper instead of O).

【0019】[0019]

【発明の効果】以上の説明から明らかなように本発明の
油脂類分解被膜の製造方法によれば、従来より孔径、多
孔度が大きく、表面の形状も凹凸に富む被膜が製造でき
るので、酸化反応に必要な酸素が多量に供給されること
になり、油脂類を低温で短時間に分解することができ
る。
EFFECTS OF THE INVENTION As is clear from the above description, according to the method for producing a fat and oil decomposition coating of the present invention, a coating having a larger pore size and porosity and a more irregular surface shape can be produced. Oxygen required for the reaction is supplied in a large amount, and oils and fats can be decomposed at low temperature in a short time.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の一実施例における工程図FIG. 1 is a process chart of an embodiment of the present invention.

【図2】同じく硬化条件を示す図FIG. 2 is a diagram showing curing conditions as well.

【図3】同じく油脂類分解被膜の断面図FIG. 3 is a sectional view of the same oil and fat decomposition film

【図4】同じく浄化率の特性図[Figure 4] Similarly, a characteristic diagram of the purification rate

【図5】同じく重量残率の特性図FIG. 5 is a characteristic diagram of weight residual ratio

【図6】従来の製造方法の工程図FIG. 6 is a process diagram of a conventional manufacturing method.

【図7】同じく硬化条件を示す図FIG. 7 is a diagram showing curing conditions similarly.

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】油脂類分解触媒として、マンガン,鉄,コ
バルトおよび銅の群から選択された一種以上の酸化物ま
たは複合酸化物を含有し、バインダーとして、金属リン
酸塩または金属ケイ酸塩を含有する塗料を調合し、前記
塗料を加熱した基材の表面に塗布し、硬化する油脂類分
解被膜の製造方法。
1. An oil or fat decomposition catalyst containing one or more oxides or complex oxides selected from the group consisting of manganese, iron, cobalt and copper, and a metal phosphate or metal silicate as a binder. A method for producing a decomposed film of fats and oils, which comprises preparing a coating material to be contained, applying the coating material to the surface of a heated substrate, and curing the coating material.
JP30301291A 1991-11-19 1991-11-19 Productiohn of lils and fats decomposing film Pending JPH05138044A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30301291A JPH05138044A (en) 1991-11-19 1991-11-19 Productiohn of lils and fats decomposing film

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30301291A JPH05138044A (en) 1991-11-19 1991-11-19 Productiohn of lils and fats decomposing film

Publications (1)

Publication Number Publication Date
JPH05138044A true JPH05138044A (en) 1993-06-01

Family

ID=17915881

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30301291A Pending JPH05138044A (en) 1991-11-19 1991-11-19 Productiohn of lils and fats decomposing film

Country Status (1)

Country Link
JP (1) JPH05138044A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009039702A1 (en) 2009-08-31 2011-03-17 Siemens Aktiengesellschaft Method for coating a substrate with a ceramic layer, comprises applying initial stage of ceramics to be produced with a solvent or dispersion agent on the substrate and evaporating the solvent or dispersion agent
JP2016034620A (en) * 2014-08-04 2016-03-17 神鋼アクテック株式会社 Metal oxide catalyst and deodorant

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102009039702A1 (en) 2009-08-31 2011-03-17 Siemens Aktiengesellschaft Method for coating a substrate with a ceramic layer, comprises applying initial stage of ceramics to be produced with a solvent or dispersion agent on the substrate and evaporating the solvent or dispersion agent
JP2016034620A (en) * 2014-08-04 2016-03-17 神鋼アクテック株式会社 Metal oxide catalyst and deodorant

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