JPH03114544A - Hydrogen peroxide decomposition catalyst - Google Patents

Hydrogen peroxide decomposition catalyst

Info

Publication number
JPH03114544A
JPH03114544A JP1250773A JP25077389A JPH03114544A JP H03114544 A JPH03114544 A JP H03114544A JP 1250773 A JP1250773 A JP 1250773A JP 25077389 A JP25077389 A JP 25077389A JP H03114544 A JPH03114544 A JP H03114544A
Authority
JP
Japan
Prior art keywords
hydrogen peroxide
transition metal
catalyst
solution
carrier
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
JP1250773A
Other languages
Japanese (ja)
Inventor
Shuzo Sakaguchi
坂口 修三
Yasuo Sugihara
杉原 康夫
Masanori Shimuta
正則 紫牟田
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.)
Mitsubishi Gas Chemical Co Inc
Original Assignee
Mitsubishi Gas Chemical Co Inc
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 Mitsubishi Gas Chemical Co Inc filed Critical Mitsubishi Gas Chemical Co Inc
Priority to JP1250773A priority Critical patent/JPH03114544A/en
Publication of JPH03114544A publication Critical patent/JPH03114544A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To obtain a hydrogen peroxide decomposition catalyst which is stable for a long period and maintains high activity by roughening the surface of a hydrophobic support to carry a transition metal. CONSTITUTION:The surface of a hydrophobic support of a metal, glass, plastic, etc., is roughened by sand blast, brushing, chemical etching, etc. A solution containing a transition metal compound dissolved in water or an organic solvent is sprayed to the surface roughened support or the support is immersed in the solution so as to carry the transition metal compound. The transition metal is uniformly distributed on the surface of a catalyst prepared in this way and hard to peel off and drop from the support and the catalyst has a high activity and stability for a long period. The catalyst is preferably used for decomposition and removal of hydrogen peroxide in a sterilization solution after sterilization of contact lens with hydrogen peroxide.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、過酸化水素分解触媒に関し、さらに詳細には
、コンタクトレンズ殺菌処理後の殺菌液中の残留過酸化
水素を分解するために好適に使用される過酸化水素分解
触媒にかかわる。
Detailed Description of the Invention [Industrial Application Field] The present invention relates to a hydrogen peroxide decomposition catalyst, and more specifically, a catalyst suitable for decomposing residual hydrogen peroxide in a sterilizing solution after contact lens sterilization treatment. Related to hydrogen peroxide decomposition catalysts used in

[従来の技術、−発明が解決しようとする問題点]過酸
化水素は殺菌、消毒および漂白などの広い分野において
使用されているが、用途によっては、使用後の過酸化水
素を分解除去することが必要とされる場合が多い。たと
えば、過酸化水素をコンタクトレンズの殺菌消毒に用い
た場合は、装着時の目への影響をなくすために、残留過
酸化水素を実質的に完全に分解する必要がある。
[Prior Art - Problems to be Solved by the Invention] Hydrogen peroxide is used in a wide range of fields such as sterilization, disinfection, and bleaching, but depending on the application, it is necessary to decompose and remove hydrogen peroxide after use. is often required. For example, when hydrogen peroxide is used to sterilize contact lenses, it is necessary to substantially completely decompose the residual hydrogen peroxide in order to eliminate the effect on the eyes when wearing the contact lenses.

一方、過酸化水素を分解除去する触媒として、P t+
 Ru、 Rh、 Ir+ Cu、 Mn、 Feおよ
びCrなどの遷移金属ならびにそれらの酸化物および水
酸化物などの化合物が有効であることは良く知られてい
る。また、それらをアルミナなどの担体に担持させた触
媒は既に市販されている。
On the other hand, as a catalyst for decomposing and removing hydrogen peroxide, P t+
It is well known that compounds such as transition metals such as Ru, Rh, Ir+Cu, Mn, Fe and Cr and their oxides and hydroxides are effective. In addition, catalysts in which they are supported on a carrier such as alumina are already commercially available.

しかしながら、アルミナおよびシリカなどの、所謂、親
水性の担体に担持させた市販触媒を使用した場合は、こ
れらの担体は表面のみならず内部まで親水性であるため
、過酸化水素を分解した後も溶液が触媒担体内部に残留
し、これが菌の繁殖を助長するためコンタクトレンズの
殺菌等の後処理用としては実用し得ないとの欠点があっ
た。
However, when commercially available catalysts supported on so-called hydrophilic carriers such as alumina and silica are used, these carriers are hydrophilic not only on the surface but also on the inside, so even after decomposing hydrogen peroxide, The problem is that the solution remains inside the catalyst carrier, which promotes the growth of bacteria, making it impractical for use in post-treatments such as contact lens sterilization.

この欠点を解消する手段として疎水性のプラスチックで
あるノリル(Noryl  ゼネラルエレクトリック社
の製品の商品名)の成形体に白金黒を担持させ、これを
コンタクトレンズ殺菌用の3z過酸化水素溶液の分解に
使用するという方法が、特公昭51−12633号公報
に開示されている。
As a means to overcome this drawback, platinum black was supported on a molded body of the hydrophobic plastic Noryl (trade name of a product manufactured by General Electric Company), and this was used to decompose a 3z hydrogen peroxide solution used for sterilizing contact lenses. A method of using this method is disclosed in Japanese Patent Publication No. 51-12633.

しかしながら、この方法では、塩化白金酸のエタノール
溶液を、表面が平滑な疎水性担体の表面に噴霧して付着
させたのち、乾燥させ、しかるのちに、塩化白金酸を水
素還元して白金黒に変化させることにより白金黒を担持
させているが、この方法では担体表面が平滑なため、塩
化白金酸の均一な付着が困難であり、従って、水素還元
の後に得られる白金黒の分布も偏析のある不均一なもの
となる。そのために、高い分解活性が得られないばかり
か、白金黒の付着力も不十分で、使用とともに白金黒が
剥離・脱落し活性が徐々に低下するといった欠点があっ
た。さらに、触媒組体であるプラスチック成形体がかな
りの容積を占める為、処理容器のコンパクト化を妨げる
といった欠点があった。
However, in this method, an ethanol solution of chloroplatinic acid is sprayed onto the surface of a smooth hydrophobic carrier, dried, and then the chloroplatinic acid is reduced with hydrogen to form platinum black. However, since the surface of the carrier is smooth, it is difficult to uniformly attach chloroplatinic acid to the carrier, and therefore the distribution of platinum black obtained after hydrogen reduction is also affected by segregation. It becomes a certain non-uniformity. For this reason, not only high decomposition activity cannot be obtained, but also the adhesion of the platinum black is insufficient, and the platinum black peels off and falls off with use, resulting in a gradual decrease in activity. Furthermore, since the plastic molded body that is the catalyst assembly occupies a considerable volume, there is a drawback that it is difficult to make the processing container more compact.

[問題点を解決するための手段] 本発明者らは、前記の如き従来技術の問題点を解決すべ
く鋭意検討を重ねた結果、表面を粗面化した疎水性担体
を用いた場合、さらに、この表面が親水化処理された疎
水性担体を用いた場合に、これらの問題点が解消される
ことを見出し、本発明を完成するに至った。すなわち本
発明は、粗面を有する疎水性担体に遷移金属を担持させ
てなることを特徴とする過酸化水素分解触媒および表面
が親水化処理された粗面を有する疎水性担体の表面に遷
移金属を担持させてなることを特徴とする過酸化水素分
解触媒である。
[Means for Solving the Problems] As a result of intensive studies to solve the problems of the prior art as described above, the present inventors found that when using a hydrophobic carrier with a roughened surface, The inventors have discovered that these problems can be solved by using a hydrophobic carrier whose surface has been treated to make it hydrophilic, and have completed the present invention. Specifically, the present invention provides a hydrogen peroxide decomposition catalyst characterized in that a transition metal is supported on a hydrophobic carrier having a rough surface, and a hydrogen peroxide decomposition catalyst characterized in that a transition metal is supported on a hydrophobic carrier having a rough surface that has been subjected to a hydrophilic treatment. This is a hydrogen peroxide decomposition catalyst characterized in that it supports a hydrogen peroxide decomposition catalyst.

本発明で使用される疎水性担体としては金属、ガラスお
よびプラスチックなどが挙げられるが、表面の粗面化が
容易な点からプラスチックが好ましく、就中、プラスチ
ックフィルム(プラスチックシートも包含される 以下
同様)が好ましい。
Examples of the hydrophobic carrier used in the present invention include metals, glass, and plastics, but plastics are preferred because they can easily roughen the surface, and among them, plastic films (including plastic sheets) are preferred. ) is preferred.

疎水性プラスチックの代表例としては、ポリエチレンテ
レフタレート、ポリカーボネート、アクリル樹脂、ポリ
スチレン、ABS樹脂、変性PPE樹脂およびポリオレ
フィンなどがある。また、疎水性が保たれれば他の樹脂
との組成物および共重合体などを使用することもできる
Representative examples of hydrophobic plastics include polyethylene terephthalate, polycarbonate, acrylic resin, polystyrene, ABS resin, modified PPE resin, and polyolefin. Furthermore, compositions and copolymers with other resins can also be used as long as hydrophobicity is maintained.

これらの疎水性プラスチックは、さらに、添加剤を含有
していてもよい。
These hydrophobic plastics may further contain additives.

処理容器のコンパクト化を可能とするために、担体を殺
菌容器内で丸めて容器内周面に密着させることが好まし
いが、そのためには、疎水性担体は、可撓性および弾性
を有するフィルム状であることが好ましい。
In order to make the processing container more compact, it is preferable to roll the carrier inside the sterilization container and bring it into close contact with the inner surface of the container. It is preferable that

これらの疎水性担体の形状には特に制限はないが、実用
上は、球状、円筒状および板状などの成形体が好ましい
Although there are no particular limitations on the shape of these hydrophobic carriers, molded bodies such as spherical, cylindrical, and plate-like shapes are practically preferred.

また、接触面積を増大させるために、さらに、これらの
疎水性担体は、波状であったり、突起および穴などが設
けられていることが好ましい。
Furthermore, in order to increase the contact area, these hydrophobic carriers are preferably wavy or provided with protrusions, holes, and the like.

疎水性担体の粗面化は、常法によって行なわれるが、実
用上、たとえば、サンドブラスト、ブラッシング、薬品
エツチングおよび炭酸カルシウムの諌り込み後の溶解エ
ツチングなどの方法を採用し得る。
The roughening of the hydrophobic carrier is carried out by conventional methods, and in practice, methods such as sandblasting, brushing, chemical etching, and solution etching after imprinting with calcium carbonate can be employed.

粗面の程度は、中心線平均粗さ(Ra)で表示した場合
に、実用上、通常は0.05μm以上、好ましくは0.
05〜50μmの範囲、特に好ましいのは0.1〜10
μmの範囲とされる。
In practice, the degree of roughness is usually 0.05 μm or more, preferably 0.05 μm or more, when expressed as center line average roughness (Ra).
The range is from 0.05 to 50 μm, particularly preferably from 0.1 to 10
It is assumed to be in the μm range.

粗面の程度が、中心線平均粗さ(Ra)で0.05μm
未満の場合には、疎水性担体に付着させた遷移金属が不
均一となり、また、付着力が小さくなり脱落・剥離し易
くなる。
The degree of roughness is 0.05 μm in center line average roughness (Ra)
If it is less than 20%, the transition metal attached to the hydrophobic carrier becomes non-uniform, and the adhesion force decreases, making it easy to fall off or peel off.

なお、本発明において、中心線平均粗さ(Ra)の定義
および測定法は、日本工業規格(JIS) B 060
11982に準拠する。
In the present invention, the definition and measurement method of center line average roughness (Ra) are based on Japanese Industrial Standards (JIS) B 060.
11982.

担持された金属の均一性と付着性を、さらに向上させる
ために、この粗面化された疎水性担体の表面が、さらに
、親水化処理される。
In order to further improve the uniformity and adhesion of the supported metal, the surface of this roughened hydrophobic support is further subjected to a hydrophilic treatment.

疎水性担体表面の親水化処理法は、担体の種類により異
なり、−概に特定し得ないが、たとえば、ポリエチレン
テレフタレートおよびポリカーボネートなどの場合には
、通常は、ヒドラジン水溶液処理およびヘキサンジアミ
ン水溶液処理などがそれぞれ有効に適用される。また、
アクリル系の防曇塗料を塗布する方法も、有効に適用さ
れる。
The hydrophilization treatment method for the surface of a hydrophobic carrier varies depending on the type of carrier, and although it cannot be generally specified, for example, in the case of polyethylene terephthalate and polycarbonate, it is usually treated with an aqueous hydrazine solution, an aqueous hexanediamine solution, etc. are validly applied. Also,
A method of applying an acrylic anti-fog paint is also effectively applied.

遷移金属成分の担持は常法によって行なわれるすなわち
、たとえば、遷移金属化合物を、水またはエタノールも
しくはアセトンなどの有機溶剤に溶解し、この溶液に粗
面化された疎水性担体を浸漬するか、または、この溶液
を粗面化された疎水性担体に噴霧するなどの方法によっ
て遷移金属化合物溶液を付着させたのち、これを乾燥す
ることによって、遷移金属化合物を担持させる。
Supporting of the transition metal component is carried out by a conventional method, for example, by dissolving the transition metal compound in water or an organic solvent such as ethanol or acetone and immersing a roughened hydrophobic support in this solution; A transition metal compound solution is applied to the roughened hydrophobic carrier by a method such as spraying this solution, and then the transition metal compound is supported by drying the solution.

この際に使用される遷移金属化合物は、水または有機溶
剤に可溶であれば特に限定されないが、ハロゲン化物、
特に塩化物が好適に使用される。
The transition metal compounds used in this case are not particularly limited as long as they are soluble in water or organic solvents, but include halides,
In particular, chlorides are preferably used.

担持された金属化合物を、通常は、水素還元、および水
素化ホウ素ナトリウムによる還元などにより単体金属に
変化させて使用されるが、遷移金属化合物のままでも使
用することができる。
The supported metal compound is usually used after being converted into an elemental metal by hydrogen reduction, reduction with sodium borohydride, etc., but the transition metal compound can also be used as it is.

本発明の触媒は、コンタクトレンズ殺菌後の殺菌液中の
残留過酸化水素を分解するために好適に使用されるほか
に、金属エツチング工場および食品工場から排出された
排液中に含有されている過酸化水素を分解するためにも
好適に使用される。
The catalyst of the present invention is suitably used to decompose residual hydrogen peroxide in a sterilizing solution after sterilizing contact lenses, and is also contained in wastewater discharged from metal etching factories and food factories. It is also suitably used to decompose hydrogen peroxide.

なお、このように使用する場合に、分解温度は、室温乃
至常温でよいが、加熱または冷却することを妨げない。
In addition, when used in this way, the decomposition temperature may be room temperature or normal temperature, but heating or cooling is not prohibited.

[実施例] 本発明の効果を実施例によりさらに具体的に説明する。[Example] The effects of the present invention will be explained in more detail with reference to Examples.

実施例1 直径20mm、厚さ5mm、面積約9c+fの変性PP
E樹脂(Noryl )のディスク状成形体の表面をサ
ンドブラスト処理により粗面化し、粗面の程度Raが2
.3μmの表面を有する粗面化担体を得た。
Example 1 Modified PP with a diameter of 20 mm, a thickness of 5 mm, and an area of about 9 c + f
The surface of the disc-shaped molded body of E resin (Noryl) was roughened by sandblasting, and the degree of roughness Ra was 2.
.. A roughened carrier having a surface of 3 μm was obtained.

これに塩化白金酸の濃度が10wtχの塩化白金酸エタ
ノール溶液を塗布し、乾燥後、80°Cで水素還元を行
ない、担体表面に白金黒を析出させて、過酸化水素分解
触媒を得た。
A chloroplatinic acid ethanol solution having a chloroplatinic acid concentration of 10 wtχ was applied to this, and after drying, hydrogen reduction was performed at 80°C to precipitate platinum black on the carrier surface to obtain a hydrogen peroxide decomposition catalyst.

この過酸化水素分解触媒の白金黒担持量は0.3mg 
/ cJであり、手指で触れても白金黒は脱落しなかっ
た。
The amount of platinum black supported on this hydrogen peroxide decomposition catalyst is 0.3 mg.
/ cJ, and the platinum black did not fall off even when touched with fingers.

このディスク状の過酸化水素分解触媒をし、ンズホルダ
ー付きのソフトコンタクトレンズ殺菌容器(容1120
mβ)に入れ、さらに、この殺菌容器に等張化剤として
NaC10,9wtL pH調節剤としてNa、llP
O4とNaH2PO,との混合物0.09wt%を含む
3wtχ過酸化水素水溶液10 mlを注入して過酸化
水素分解テストを行なった。
This disk-shaped hydrogen peroxide decomposition catalyst is used in a soft contact lens sterilization container with lens holder (capacity 1120
mβ), and in this sterilized container, add 10.9wtL of NaCl as an isotonic agent and Na, llP as a pH adjuster.
A hydrogen peroxide decomposition test was performed by injecting 10 ml of a 3 wt χ hydrogen peroxide aqueous solution containing 0.09 wt % of a mixture of O4 and NaH2PO.

こめ液の過酸化水素の濃度が1100ppに低下するま
でに要した時間は3.2時間であり、これは分解試験を
100回繰り返した後も変わらなかった。
The time required for the concentration of hydrogen peroxide in the boiling solution to drop to 1100 pp was 3.2 hours, and this remained unchanged even after the decomposition test was repeated 100 times.

実施例2 36mm X 9mm 、厚さ0.1mm、片面の面積
9.4cfflのポリエチレンテレフタレートフィルム
の片面をサンドブラスト処理により粗面化し、粗面の程
度Raが3.4μmの表面を有する粗面化担体を得た。
Example 2 One side of a polyethylene terephthalate film measuring 36 mm x 9 mm, 0.1 mm thick, and 9.4 cffl on one side was roughened by sandblasting, and the roughened carrier had a surface with a roughness level Ra of 3.4 μm. I got it.

さらに、この粗面化担体を、30w tχのヒドラジン
水溶液に80°Cで30分間浸漬して粗面化担体の表面
の親水化処理を行なった。
Furthermore, this roughened carrier was immersed in an aqueous hydrazine solution of 30wtχ at 80°C for 30 minutes to make the surface of the roughened carrier hydrophilic.

この表面が親水化処理された粗面化担体の表面に塩化白
金酸の濃度10wtχの塩化白金酸エタノール溶液を塗
布し、乾燥後、80°Cで水素還元を行ない、この担体
の表面に白金黒を析出させて、過酸化水素分解触媒を得
た。
A chloroplatinic acid ethanol solution with a concentration of 10 wtχ is applied to the surface of the roughened carrier whose surface has been made hydrophilic, and after drying, hydrogen reduction is performed at 80°C to coat the surface of the carrier with platinum black. was precipitated to obtain a hydrogen peroxide decomposition catalyst.

この過酸化水素分解触媒の白金黒担持量は0.24mg
/c+flであり、この過酸化水素触媒は可撓性を保っ
ており、さらに、析出した白金黒がフィルム表面に均一
に付着していることが観察された。
The amount of platinum black supported on this hydrogen peroxide decomposition catalyst is 0.24 mg.
/c+fl, and this hydrogen peroxide catalyst maintained flexibility, and furthermore, it was observed that precipitated platinum black was uniformly attached to the film surface.

この過酸化水素分解触媒をレンズホルダー付きのソフト
コンタクトレンズ殺菌容器(容量18mβ)に、遷移金
属担持面を内面とし殺菌容器の内周面に密着するように
入れ、さらに、この殺菌容器に等張化剤としてNaCl
0.9wtX、 pH4j1節剤としてNaH2O4と
Na)12Po4 との混合物0.09wtχを含む3
w tX過酸化水素水溶液10m1を注入して過酸化水
素分解テストを行なった。
This hydrogen peroxide decomposition catalyst was placed in a soft contact lens sterilization container (capacity 18 mβ) equipped with a lens holder so that the transition metal-supporting surface was on the inside and closely contacted the inner peripheral surface of the sterilization container, and the sterilization container was then isostatically NaCl as a oxidizing agent
0.9 wt
A hydrogen peroxide decomposition test was conducted by injecting 10 ml of wtX hydrogen peroxide aqueous solution.

過酸化水素の濃度が1100ppに低下するまでに要し
た時間は262時間であり、これは分解試験を100回
繰り返した後も変わらなかった。
The time required for the concentration of hydrogen peroxide to drop to 1100 pp was 262 hours, and this remained unchanged even after repeating the decomposition test 100 times.

この際、過酸化水素分解触媒の担体をフィルム状とした
ことにより触媒の体積が大幅に減少したため、殺菌容器
をコンパクトなものにすることができた。
At this time, by using a film-like carrier for the hydrogen peroxide decomposition catalyst, the volume of the catalyst was significantly reduced, so the sterilization container could be made more compact.

また、この過酸化水素分解触媒は可撓性および弾性を有
し、殺菌容器内ヘセットする際、その可撓性と弾性とに
より容器の内面に密着せしめられ、また、着脱も極めて
容易であった。
In addition, this hydrogen peroxide decomposition catalyst has flexibility and elasticity, and when it is set in a sterilization container, its flexibility and elasticity allow it to adhere tightly to the inner surface of the container, and it is also extremely easy to attach and detach. .

比較例1 担体の表面を粗面化せず、そのまま使用した以外は実施
例1と同様に操作した。
Comparative Example 1 The same procedure as in Example 1 was carried out except that the surface of the carrier was not roughened and was used as it was.

得られた過酸化水素分解触媒の白金黒担持量は0.3■
/cfflであったが、担持状態は不均一で、かつ、手
指で軽く触れただけで白金黒が容易に剥離・脱落した。
The amount of platinum black supported on the obtained hydrogen peroxide decomposition catalyst was 0.3■
/cffl, but the supported state was non-uniform, and the platinum black easily peeled off and fell off even when touched lightly with fingers.

過酸化水素の濃度が1100ppまでに要した時間は初
回4.8時間であったが、徐々に活性が低下し、100
回目の時点では6.3時間にまで低下した。
The time required for the concentration of hydrogen peroxide to reach 1100pp was 4.8 hours the first time, but the activity gradually decreased and the concentration reached 100pp.
At the second time, the time had decreased to 6.3 hours.

[発明の効果コ 本発明の過酸化水素分解触媒は、担持された遷移金属成
分が、担体の表面に均一に分布し、担体からの遷移金属
成分の剥離・脱落が少なく、長期間にわたって高活性が
維持されるので、長期間にわたり安定して使用すること
ができる。また、担体内部が疎水性の為、分解後の溶液
が担体内部に残留して苗が繁殖することがない。従って
、本発明の過酸化水素分解触媒は、コンタクトレンズを
過酸化水素殺菌した後の殺菌液中の過酸化水素を分解除
去するために好適に使用される他に、過酸化水素を含有
する排液中などの処理にも好適に使用し得るものである
[Effects of the Invention] The hydrogen peroxide decomposition catalyst of the present invention has a supported transition metal component uniformly distributed on the surface of the carrier, less peeling and falling off of the transition metal component from the carrier, and high activity over a long period of time. is maintained, so it can be used stably for a long period of time. Furthermore, since the inside of the carrier is hydrophobic, the solution after decomposition will not remain inside the carrier and seedlings will not propagate. Therefore, the hydrogen peroxide decomposition catalyst of the present invention is suitably used for decomposing and removing hydrogen peroxide in a sterilizing solution after contact lenses are sterilized with hydrogen peroxide. It can also be suitably used for processing in liquid.

Claims (1)

【特許請求の範囲】 1、粗面を有する疎水性担体に遷移金属を担持させてな
ることを特徴とする過酸化水素分解触媒。 2、表面が親水化処理された粗面を有する疎水性担体の
表面に遷移金属を担持させてなることを特徴とする過酸
化水素分解触媒。
[Scope of Claims] 1. A hydrogen peroxide decomposition catalyst characterized by having a transition metal supported on a hydrophobic carrier having a rough surface. 2. A hydrogen peroxide decomposition catalyst characterized in that a transition metal is supported on the surface of a hydrophobic carrier having a rough surface treated to make the surface hydrophilic.
JP1250773A 1989-09-28 1989-09-28 Hydrogen peroxide decomposition catalyst Pending JPH03114544A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1250773A JPH03114544A (en) 1989-09-28 1989-09-28 Hydrogen peroxide decomposition catalyst

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1250773A JPH03114544A (en) 1989-09-28 1989-09-28 Hydrogen peroxide decomposition catalyst

Publications (1)

Publication Number Publication Date
JPH03114544A true JPH03114544A (en) 1991-05-15

Family

ID=17212828

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1250773A Pending JPH03114544A (en) 1989-09-28 1989-09-28 Hydrogen peroxide decomposition catalyst

Country Status (1)

Country Link
JP (1) JPH03114544A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009536873A (en) * 2006-05-12 2009-10-22 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 Carrier for treating exhaust gas with dispersed catalyst
JPWO2017010277A1 (en) * 2015-07-10 2017-07-20 株式会社武蔵野化学研究所 Manufacturing method of organic acid ester liquid, and manufacturing method of resist solvent for electronic component manufacturing or rinsing liquid for electronic component manufacturing
JP2017159228A (en) * 2016-03-09 2017-09-14 国立大学法人大阪大学 Decomposition catalyst for hydrogen peroxide for sterilization of contact lens and manufacturing method therefor

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009536873A (en) * 2006-05-12 2009-10-22 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 Carrier for treating exhaust gas with dispersed catalyst
JPWO2017010277A1 (en) * 2015-07-10 2017-07-20 株式会社武蔵野化学研究所 Manufacturing method of organic acid ester liquid, and manufacturing method of resist solvent for electronic component manufacturing or rinsing liquid for electronic component manufacturing
US10632456B2 (en) 2015-07-10 2020-04-28 Musashino Chemical Laboratory, Ltd. Process for producing organic acid ester-type liquid, and process for producing solvent of resist for producing electronic part or rinsing liquid for producing electronic parts
JP2017159228A (en) * 2016-03-09 2017-09-14 国立大学法人大阪大学 Decomposition catalyst for hydrogen peroxide for sterilization of contact lens and manufacturing method therefor

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