JPS61247604A - Oxygen generator - Google Patents
Oxygen generatorInfo
- Publication number
- JPS61247604A JPS61247604A JP60084575A JP8457585A JPS61247604A JP S61247604 A JPS61247604 A JP S61247604A JP 60084575 A JP60084575 A JP 60084575A JP 8457585 A JP8457585 A JP 8457585A JP S61247604 A JPS61247604 A JP S61247604A
- Authority
- JP
- Japan
- Prior art keywords
- hydrogen peroxide
- oxygen
- gas
- decomposing catalyst
- gaseous
- 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
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
Description
【発明の詳細な説明】
(技術分野)
本発明は過酸化水素あるいは過酸化水素付加物から分解
触媒を用いて酸素ガスを発生する酸素発生装置に関する
。DETAILED DESCRIPTION OF THE INVENTION (Technical Field) The present invention relates to an oxygen generator that generates oxygen gas from hydrogen peroxide or a hydrogen peroxide adduct using a decomposition catalyst.
(従来技術)
従来より酸素発生方法としてはHFe HCu +Ni
、 Co、 Mn、 Cr、 Pb、 V、 W、又
はその化合物の中から選ばれた1種以上の触媒の懸濁液
あるいは水浴液と、過炭酸ソーダとを接触させて酸素ガ
スを発生する方法(特開IJ@54−26990)、炭
屓ソーダと過敏化水素との付加化合物と、触媒として用
いる二酸化マンガンまたは鉄、鋼。(Prior art) Conventional oxygen generation methods include HFe HCu +Ni
, Co, Mn, Cr, Pb, V, W, or a compound thereof, a suspension or a water bath liquid of one or more catalysts is brought into contact with sodium percarbonate to generate oxygen gas. (Japanese Patent Application Laid-open No. IJ@54-26990), an addition compound of charcoal soda and sensitizing hydrogen, and manganese dioxide or iron or steel used as a catalyst.
鉛などの金属塩を濃度の異なるアラビアゴムにより固化
せしめた溶解度の異なる複数種の水溶性固形物とを混合
した混合物に水を加えて一定量の酸素を長時間継続して
発生せしめるようにした酸素発生方法(%開昭58−1
90804)、さらに過炭酸ナトリウム(2NazCO
r3H*Ot)に水を加え酸素全発生させるに当って、
触媒として用いる二酸化マンガン、または鉄、鋼、鉛な
どの金属塩の粉末を、ポリビニールアルコールによって
、水中に於ての崩壊時間が、それぞれ異なる固結物を造
り、これを過炭酸ナトリウムに前身って混入しておき、
適量の水を加えることにより、過炭酸ナトリウムが、急
激に酸素を発生することなく、一定時間内にコンスタン
トに酸素を発生するようにした酸素発生方法(特開昭5
7−160902)などが知られている。Water is added to a mixture of metal salts such as lead solidified with gum arabic at different concentrations and multiple types of water-soluble solids with different solubility to continuously generate a certain amount of oxygen over a long period of time. Oxygen generation method (% Kaisho 58-1
90804), and further sodium percarbonate (2NazCO
When adding water to r3H*Ot) to generate all oxygen,
Powders of manganese dioxide or metal salts such as iron, steel, and lead used as catalysts are mixed with polyvinyl alcohol to form solids with different disintegration times in water, and this is mixed with sodium percarbonate. Mix it with
An oxygen generation method (Japanese Unexamined Patent Publication No. 1983-1992) in which sodium percarbonate constantly generates oxygen within a certain period of time by adding an appropriate amount of water, without rapidly generating oxygen.
7-160902) and the like are known.
またペルオクソ炭酸アルカリ塩(塩基性)とベルオクソ
ニ硫酸塩のごとき酸性ペルオクソ酸性塩全夫々水に接触
して散票全発生せしめ、酸素発生後の残留物を混合して
廃液を中和させることも提案されている。It is also proposed that acidic peroxo acid salts such as alkali peroxo carbonate (basic) and peroxoni sulfate are brought into contact with water to generate dust, and the residue after oxygen generation is mixed to neutralize the waste liquid. has been done.
しかして過酸化水素水あるいは過酸化水素付加物から分
解触媒を用いて酸素ガスを得る方法において、発生する
気体の大部分は酸素であるが一部過酸化水素が酸素と水
に分解されずに過酸化水素のまま気化することがある。However, in the method of obtaining oxygen gas from hydrogen peroxide solution or hydrogen peroxide adduct using a decomposition catalyst, most of the gas generated is oxygen, but some hydrogen peroxide is not decomposed into oxygen and water. May evaporate as hydrogen peroxide.
得られた酸素ガスの用途によってはこの混合気体のまま
で使用できることもあるが、過酸化水素の酸化力が大き
いために整置な招くことがしばしばあるO
また、過酸化水素水を取扱う場所においては、大気中に
気化した過酸化水素を含むことがあるが、過酸化水素ガ
スが大気中に1 ppm以上含む場合、人体に悪影Wを
及はすと言われている。Depending on the purpose of the obtained oxygen gas, it may be possible to use it as a mixed gas, but due to the strong oxidizing power of hydrogen peroxide, it is often necessary to store it properly. Although the atmosphere may contain vaporized hydrogen peroxide, it is said that if hydrogen peroxide gas is contained in the atmosphere at 1 ppm or more, it will have an adverse effect on the human body.
このように空気中の微量の過酸化水素ガスを除去する方
法として、たとえば水中へこの混合気体を通し水へ吸収
させる方法がある。この方法では大量の水を使う装置が
心安である。このため雰囲気空気の浄化のためには簡便
なフィルタ一方式が望ましい。As a method for removing trace amounts of hydrogen peroxide gas from the air, there is, for example, a method of passing this gas mixture into water and absorbing it into the water. This method is safe for devices that use large amounts of water. Therefore, a simple filter type is desirable for purifying the atmospheric air.
(発明の目的)
本発明は上記の要望にもとづいて提案されたもので、フ
ィルタ一式の過酸化水素ガス除去による酸素発生装置を
提供することを目的とするものである。(Object of the Invention) The present invention was proposed based on the above-mentioned needs, and an object of the present invention is to provide an oxygen generation device using a set of filters for removing hydrogen peroxide gas.
(発明の開示)
過酸化水素は、沸点151℃(1気圧への外挿値)であ
るが室温においても数mm Hg (2g℃で1.3
mm Hg )の蒸気圧をもっている。従って飽和状態
では、O11容積%以上の濃度になる可能性もある。人
体への許容濃度は1・〜2ppmであると言われている
。人体に触れる雰囲気中の過酸化濃度を許容濃度以下に
するためには一般に100 □。。。の濃度にまで下
げなければならない。(Disclosure of the Invention) Hydrogen peroxide has a boiling point of 151°C (extrapolated to 1 atm), but even at room temperature it has a boiling point of several mm Hg (1.3 g at 2g°C).
It has a vapor pressure of mm Hg). Therefore, in a saturated state, there is a possibility that the concentration of O11% by volume or more. The permissible concentration for the human body is said to be 1.-2 ppm. In general, 100 □ is required to reduce the peroxide concentration in the atmosphere that comes into contact with the human body to below the permissible concentration. . . must be reduced to a concentration of
過酸化水素は強力な酸化剤であり、また化学的に比較的
不安定である性質をもっている。本発明ではこれらの性
質を利用して目的とするフイルタ一式の浄化方式全検討
した。Hydrogen peroxide is a strong oxidizing agent and is relatively chemically unstable. In the present invention, all purification methods for a set of filters have been investigated by utilizing these properties.
1つの方式は、過酸化水素は自らも分解しやすいが、触
媒的に促進して分解反応がおこる。One method is to promote the decomposition reaction catalytically, although hydrogen peroxide is easily decomposed by itself.
この目的に使用される触媒としては、白金、パラジウム
、金、銀などの重金属のコロイドなど比表面積が大きい
金属粉あるいは酸化コバルト。Catalysts used for this purpose include metal powders with a large specific surface area, such as colloids of heavy metals such as platinum, palladium, gold, and silver, or cobalt oxide.
酸化マンガンなどの金属酸化物あるいはアルカリ水など
が挙げられる。Examples include metal oxides such as manganese oxide and alkaline water.
他の方法としては、過酸化水素は酸化力が太きいために
還元性の物質を過酸化水素を含む混合気体に接触させる
ことによって分解消滅させることである。還元性物質と
しては活性炭の粒嗜粉、アスコルビン酸、チオ硫酸ナト
リウムなどが適当であるが特にこれらに限定しなくても
よい。Another method is to decompose and eliminate a reducing substance by bringing it into contact with a gas mixture containing hydrogen peroxide, since hydrogen peroxide has a strong oxidizing power. Suitable reducing substances include activated carbon powder, ascorbic acid, sodium thiosulfate, etc., but are not particularly limited to these.
(実施例)
(1)5%過酸化水素水に二酸化マンガン粉末會聞分の
1量加えて発生する酸素ガス中には0.15容量チの過
酸化水素ガスを含んでいる。(Example) (1) The oxygen gas generated by adding one amount of manganese dioxide powder to a 5% hydrogen peroxide solution contains 0.15 volumes of hydrogen peroxide gas.
この混合気体を、重量比で木綿セルロース100部、二
酸化マンガン粉末10部の混合物を木綿布で両面から包
んで厚さ2mのフィルタ(0,05t / c、rA
) k通したとコロ通過シタカス中の過酸化水素ガス濃
度は1 pI)m以下であった。This gas mixture was filtered into a 2m thick filter (0.05t/c, rA
) The concentration of hydrogen peroxide gas in the shitacus that passed through the roller was less than 1 pI)m.
(2) (1)と同じように発生させた過酸化水素を
含む酸素ガス中の過酸化水素除去のために、0.1〜5
謔大の活性炭粒をポリエステル繊維の不織布でつくった
袋につめて厚さ1cInのフィルターとして、これに上
記混合気体tmすと過酸化水素濃度は2 ppmであっ
た。(2) To remove hydrogen peroxide from the oxygen gas containing hydrogen peroxide generated in the same way as in (1),
When large-sized activated carbon particles were packed in a bag made of non-woven polyester fiber to form a 1 cIn thick filter, and the above mixed gas tm was poured into the bag, the hydrogen peroxide concentration was 2 ppm.
(3) (2)の実験において、活性炭粒にアスコル
ビン酸を聞分の1m混合したものでは通過したガス中の
過酸化水素濃度は1 ppm以下であった〇
(発明の効果)
本発明は叙上のように、過酸化水素あるいは過酸化水素
付加物から分解触媒を用いて酸素ガスを発生するために
用いられ、重金属粉。(3) In the experiment in (2), when activated carbon granules were mixed with ascorbic acid for 1 m, the hydrogen peroxide concentration in the passing gas was 1 ppm or less. As above, it is used to generate oxygen gas from hydrogen peroxide or hydrogen peroxide adducts using a decomposition catalyst, and heavy metal powder.
金属酸化物粉などの分解触媒および、もしくは活性炭、
アスコルビン酸、チオ硫酸ソーダなどの還元性物質を保
持させたフィルターを内蔵せしめ発生する酸素ガスを前
記のフィルターを通すことにより、酸素ガス中の過酸化
水素を極めて効率よく除去しうる効果を有するものであ
る。Decomposition catalyst such as metal oxide powder and/or activated carbon,
A device that has a built-in filter that retains reducing substances such as ascorbic acid and sodium thiosulfate, and has the effect of extremely efficiently removing hydrogen peroxide from the oxygen gas by passing the generated oxygen gas through the filter. It is.
Claims (1)
いて酸素ガスを発生するために用いられ、重金属粉、金
属酸化物粉などの分解触媒および、もしくは活性炭、ア
スコルビン酸、チオ硫酸ソーダなどの還元性物質を保持
させたフィルターを内蔵せしめた酸素発生装置。Used to generate oxygen gas from hydrogen peroxide or hydrogen peroxide adducts using decomposition catalysts, such as heavy metal powders, metal oxide powders, etc., and/or reduction of activated carbon, ascorbic acid, sodium thiosulfate, etc. An oxygen generator with a built-in filter that retains harmful substances.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60084575A JPS61247604A (en) | 1985-04-22 | 1985-04-22 | Oxygen generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP60084575A JPS61247604A (en) | 1985-04-22 | 1985-04-22 | Oxygen generator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS61247604A true JPS61247604A (en) | 1986-11-04 |
Family
ID=13834470
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP60084575A Pending JPS61247604A (en) | 1985-04-22 | 1985-04-22 | Oxygen generator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS61247604A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5348724A (en) * | 1992-06-11 | 1994-09-20 | Toshin Chemical Industry Co., Ltd. | Method of decomposing hydrogen peroxide |
US5549833A (en) * | 1992-06-11 | 1996-08-27 | Toshin Chemical Industry Co., Ltd. | Method of decomposing hydrogen peroxide |
-
1985
- 1985-04-22 JP JP60084575A patent/JPS61247604A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5348724A (en) * | 1992-06-11 | 1994-09-20 | Toshin Chemical Industry Co., Ltd. | Method of decomposing hydrogen peroxide |
US5549833A (en) * | 1992-06-11 | 1996-08-27 | Toshin Chemical Industry Co., Ltd. | Method of decomposing hydrogen peroxide |
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