JPS62297201A - Oxygen generator - Google Patents

Oxygen generator

Info

Publication number
JPS62297201A
JPS62297201A JP14163086A JP14163086A JPS62297201A JP S62297201 A JPS62297201 A JP S62297201A JP 14163086 A JP14163086 A JP 14163086A JP 14163086 A JP14163086 A JP 14163086A JP S62297201 A JPS62297201 A JP S62297201A
Authority
JP
Japan
Prior art keywords
hydrogen peroxide
oxygen
decomposition reaction
resistant
bottle
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.)
Granted
Application number
JP14163086A
Other languages
Japanese (ja)
Other versions
JPH0428641B2 (en
Inventor
Sosuke Oriya
織家 荘介
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.)
DAIWA GIKEN KK
Original Assignee
DAIWA GIKEN KK
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 DAIWA GIKEN KK filed Critical DAIWA GIKEN KK
Priority to JP14163086A priority Critical patent/JPS62297201A/en
Publication of JPS62297201A publication Critical patent/JPS62297201A/en
Publication of JPH0428641B2 publication Critical patent/JPH0428641B2/ja
Granted legal-status Critical Current

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  • Oxygen, Ozone, And Oxides In General (AREA)

Abstract

PURPOSE:To generate a large amount of O2 continuously for a long time, by dripping H2O2 on a powder catalyst put in a decomposition reaction column consisting of a chemical-resistant and heat-resistant filtering material having a fine porous filtering face and cooling generated steam and O2. CONSTITUTION:A powder catalyst 12 such as MnO2, etc., is put in the bottom of a bottomed decomposition reaction column 2 consisting of a chemical-resistant and heat-resistant filtering material 11 having fine porous filtering face. Then a suction needle 27 connected to a silicon tube 21 set in a circular dent 20 formed in the inner wall face of a pump 3 is inserted into a central thrusting part 29 of a cap 28 of a bottle 4 having H2O2. Then a motor 22 is operated, the tube 21 is squeezed by pressing rollers 24 set between outer peripheral parts of two discs 23, H2O2 is sucked and fed through a feed pipe 13 of a reaction column 2 on a catalyst 12 to generate steam and O2. Then generated steam and O2 are introduced from a main body 1 to a riser and also used as a coller 5, cooled by cold air sent from a cooling fan 9 to an air conduit 33, water is dropped on a storage measure 7 and O2 is exhausted from a feed pipe 8.

Description

【発明の詳細な説明】 3、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を触媒による分解反応によって酸素
を発生せしめる酸素発生装置に関するものである。
Detailed Description of the Invention 3. Detailed Description of the Invention [Field of Industrial Application] The present invention relates to an oxygen generating device that generates oxygen by decomposing hydrogen peroxide using a catalyst.

〔発明の背景〕 一般に、狭心症、心筋梗塞、喘息、肺気腫。[Background of the invention] Generally, angina pectoris, myocardial infarction, asthma, emphysema.

肺癌、川崎病等による心臓発作に対しては酸素吸入が効
果的といわれている。特に、老齢化の進む中でその必要
性が高い、また、酸素吸入がスポーツや重労働後の疲労
回復、疲れた頭脳の活性化にも効果的といわれている。
Oxygen inhalation is said to be effective against heart attacks caused by lung cancer, Kawasaki disease, etc. This is especially important as we age, and oxygen inhalation is said to be effective in recovering from fatigue after sports or hard labor, and in activating a tired brain.

このため。For this reason.

各種の酸素発生装置の開発が行われている。Various oxygen generators are being developed.

ところが、いずれも高価格であり、酸素発生量が少ない
し、酸素発生時間も短い、しかも。
However, all of these methods are expensive, generate only a small amount of oxygen, and take only a short time to generate oxygen.

酸素発生量の増減調整ができず1発生途中で中断させた
り、再発生させることができない等の種々の問題があっ
た。
There have been various problems such as the inability to increase or decrease the amount of oxygen generated, the generation being interrupted midway through generation, and the generation being unable to be restarted.

〔発明の目的〕[Purpose of the invention]

本発明は上記種々の問題を解消するためのもので、低価
格で入手できる過酸化水素を発生源とし、酸素発生量が
多く、長時間継続して発注させることが可能であり、し
かも、病状等に応じて酸素の発生量を自由に調整できる
ことは勿論、酸素発生途中で中断したり、再発生させる
ことも可能な酸素発生装置を提供することを目的として
いる。また、他の目的は過酸化水素瓶を他の供給皿等よ
り入れ替える必要なく、そのまま着装できる至便性の高
い酸素発生装置を提供することにある。
The present invention is intended to solve the various problems mentioned above.It uses hydrogen peroxide, which is available at a low price, as a generation source, generates a large amount of oxygen, and can be ordered continuously for a long time. It is an object of the present invention to provide an oxygen generating device that can not only freely adjust the amount of oxygen generated depending on the situation, but also can interrupt oxygen generation midway through and restart oxygen generation. Another object of the present invention is to provide a highly convenient oxygen generator that can be attached as is without the need to replace the hydrogen peroxide bottle with another supply tray or the like.

〔発明の構成〕[Structure of the invention]

上記目的を達成するため2本発明は、過酸化水素を触媒
による分解反応によって酸素を発生せしめる酸素発生装
置において、微細な多孔濾過面を有する耐薬・耐熱性の
濾過材よりなる分解反応筒と、該分解反応筒に収容した
粉末触媒に過酸化水素を滴下せしめる供給手段と、前記
分解反応筒内で発生し、その筒壁より放散した水蒸気酸
素を冷却するクーラーとを備え1手軽に多量の酸素が安
価に得られるように構成したものである。
In order to achieve the above object, the present invention provides an oxygen generating device that generates oxygen through a decomposition reaction of hydrogen peroxide using a catalyst; A supply means for dropping hydrogen peroxide onto the powdered catalyst housed in the decomposition reaction cylinder, and a cooler for cooling water vapor oxygen generated in the decomposition reaction cylinder and dissipated from the cylinder wall, are provided. It is constructed so that it can be obtained at low cost.

なお、過酸化水素を触媒による分解反応によって酸素を
発生せしめるこ、とは公知であるが。
Incidentally, it is known that oxygen is generated by a decomposition reaction of hydrogen peroxide using a catalyst.

過酸化水素の濃度、触媒の活性化の優劣差によりその発
生状況は大いに異なる。
The situation in which it occurs varies greatly depending on the concentration of hydrogen peroxide and the degree of activation of the catalyst.

本発明の場合は。In the case of the present invention.

2 HzOz+触媒−2820+ Ox  +46.9
00KclIL2hes   (22,4LX!>  
  329   (!l  41)の如く強い発熱反応
であるが、小中学校の指導要領のように、極く濃度の低
い5%程度の過酸化水素に活性化の低い天然性の二酸化
マンガン粉を投下すると、徐々に分解して酸素を発生す
るが、95%の多量の希薄水に発生熱は吸収され2分解
水及び発生酸素ガスの温度上昇も殆ど認められない位い
分解反応は穏やかである。
2 HzOz+Catalyst -2820+Ox +46.9
00KclIL2hes (22,4LX!>
329 (!l 41), it is a strong exothermic reaction, but if you drop natural manganese dioxide powder with low activation into hydrogen peroxide at an extremely low concentration of about 5%, as in the curriculum guidelines for elementary and junior high schools. , it gradually decomposes and generates oxygen, but the heat generated is absorbed by the 95% large amount of diluted water, and the decomposition reaction is so gentle that there is hardly any temperature rise of the decomposed water and the generated oxygen gas.

また、電解法によって得られる高純度で活性化のいたっ
て高い二酸化マンガン等の粉末の上に食品添加物用とし
て広く一般に市販されている比較的濃度の高い35%過
酸化水素(麺類。
In addition, on top of the highly purified and highly activated manganese dioxide powder obtained by electrolysis, a relatively high concentration of 35% hydrogen peroxide (noodles), which is widely commercially available as a food additive, is added.

すり身用魚類、漬物野菜等の漂白用)を滴下又は逆に、
過酸化水素に二酸化マンガン粉を入れる0両者が接触し
た瞬間爆発的に分解反応を生じ、その分解熱で生じた多
量の水蒸気と酸素が触媒粉を伴って吹上げ、瞬時に1分
解反応は終了する。容器中に残った液は沸騰状態にあり
For bleaching fish for surimi, pickled vegetables, etc.) or vice versa,
Adding manganese dioxide powder to hydrogen peroxide 0 An explosive decomposition reaction occurs the moment the two come into contact, and a large amount of water vapor and oxygen generated by the decomposition heat blows up along with the catalyst powder, and the decomposition reaction ends instantly. do. The liquid remaining in the container is in a boiling state.

過酸化水素の濃度、二酸化マンガンの粒度、活性化、純
度の如何により分解能力、速度1発生状況に大いに差異
がある。
There are great differences in decomposition ability and rate 1 generation depending on the concentration of hydrogen peroxide, particle size, activation, and purity of manganese dioxide.

〔実施例〕〔Example〕

次に1本発明の実施例を図面に基づいて説明する。 Next, an embodiment of the present invention will be described based on the drawings.

第1図は本発明装置の全体図を示すもので。FIG. 1 shows an overall view of the device of the present invention.

図において、lは本体、2は収容した触媒に過酸化水素
を滴下して分解反応を生じさせることにより酸素を発生
する分解反応筒、3は過酸化水素の供給ポンプ、4は過
酸化水素瓶、5は前記分解反応筒2で発生した高温の酸
素ガス及び水蒸気の上昇管兼クーラー、6は上昇管5に
連通した螺旋管よりなるクーラー、7はコンデンスした
水を集める溜枡、8は吸入マスク部(図示せず)への酸
素送気バイブ、9は前記クーラー5及び6の冷却用ファ
ン、10は本体1及び溜枡7内の水を抜き取るコックで
ある。
In the figure, l is the main body, 2 is a decomposition reaction cylinder that generates oxygen by dropping hydrogen peroxide onto the catalyst contained in it to cause a decomposition reaction, 3 is a hydrogen peroxide supply pump, and 4 is a hydrogen peroxide bottle. , 5 is a rising pipe and cooler for the high temperature oxygen gas and water vapor generated in the decomposition reactor 2, 6 is a cooler consisting of a spiral tube communicating with the rising pipe 5, 7 is a reservoir for collecting condensed water, and 8 is an intake pipe. 9 is a cooling fan for the coolers 5 and 6; 10 is a cock for draining water from the main body 1 and the reservoir 7;

前記分解反応筒2は第3図に示す如く微細な多孔質の濾
過構造を有するセラミソイ!またはガラスフィルタ等の
耐過酸化水素、耐熱性のある濾過材11により有底筒状
に形成し、その底部に高活性化粉末触媒12を入れ、そ
の上に過酸化水素供給管13の下部末端に取付けた分散
板14を位置せしめ、その上を粉末触媒12の飛散防止
用のガラスウールやその他のフィルタ材15で覆い、更
に、その上を多孔板16で軽く押えてなる。この分解反
応筒2は一定の酸素の発生に必要な粉末触媒12の収容
量に対して容積を数倍以上に大きくシ、筒内で発生した
水蒸気酸素を一時的に保留する大きな空間を備え得るよ
うにしたものである。また、粉末触媒12を収容した分
解反応筒2の開放された頂部には中央に前記過酸化水素
供給管13を貫通せしめた保持体18が嵌着している。
The decomposition reaction column 2 is made of ceramic soy which has a fine porous filtration structure as shown in FIG. Alternatively, a cylindrical shape with a bottom is formed using a hydrogen peroxide-resistant and heat-resistant filter material 11 such as a glass filter, a highly activated powder catalyst 12 is placed in the bottom part, and the lower end of the hydrogen peroxide supply pipe 13 is placed on top of the highly activated powder catalyst 12. The dispersion plate 14 attached to the dispersion plate 14 is positioned, the top thereof is covered with glass wool or other filter material 15 for preventing scattering of the powdered catalyst 12, and the top thereof is further lightly pressed with a porous plate 16. The decomposition reactor cylinder 2 has a capacity several times larger than the capacity of the powder catalyst 12 required to generate a certain amount of oxygen, and can be provided with a large space for temporarily retaining the water vapor and oxygen generated within the cylinder. This is how it was done. Further, a holder 18 through which the hydrogen peroxide supply pipe 13 passes is fitted in the center of the open top of the decomposition reaction cylinder 2 containing the powdered catalyst 12.

該保持体18は過酸化水素供給管13が貫通する中央環
18aと9分解反応筒2の頂部に嵌合できるる外周部1
8bとの間をリム17で結合した構造にし。
The holder 18 includes a central ring 18a through which the hydrogen peroxide supply pipe 13 passes, and an outer peripheral portion 1 that can fit into the top of the 9-decomposition reaction cylinder 2.
8b is connected by a rim 17.

前記過酸化水素供給管13と分解反応筒2を固着保持せ
しめるためのものである。
This is for holding the hydrogen peroxide supply pipe 13 and the decomposition reaction tube 2 firmly together.

19は保持体18の下部に取付けたフィルタである。19 is a filter attached to the lower part of the holder 18.

上記のように構成した分解反応筒2内に収容した粉末触
媒12上に過酸化水素供給管13を通して過酸化水素を
供給すると、過酸化水素は分散Fi14によって触媒1
2上に広く滴下されて触媒と接触し、同時に分解反応を
生じる。その分解反応熱によって生じた多量の水蒸気と
酸素は分解反応筒2内の広い1.ri、過構造体9即ち
When hydrogen peroxide is supplied through the hydrogen peroxide supply pipe 13 onto the powder catalyst 12 housed in the decomposition reactor 2 configured as described above, the hydrogen peroxide is dispersed into the catalyst 1 by the dispersion Fi 14.
It is widely dropped onto 2 and comes into contact with the catalyst, causing a decomposition reaction at the same time. A large amount of water vapor and oxygen generated by the heat of the decomposition reaction are transferred to the large 1. ri, overstructure 9 ie.

フィルタ材15とフィルタ19で囲まれた空間内に広が
り、容易に多量の水蒸気と酸素を分解反応筒2外(本体
1内)へ発散して分解反応筒2内の圧力の低下を図り8
分解反応時に関与しなかった過酸化水素の水及び過酸化
水素の一部は触媒層を降下しながら分解反応を生じ1分
離した水は分解反応筒2の底部より本体1内底部に水滴
となって落下する。
It spreads in the space surrounded by the filter material 15 and the filter 19, and easily releases a large amount of water vapor and oxygen to the outside of the decomposition reaction cylinder 2 (inside the main body 1), thereby reducing the pressure inside the decomposition reaction cylinder 2.
The water of hydrogen peroxide that did not participate in the decomposition reaction and a part of the hydrogen peroxide undergo a decomposition reaction while descending down the catalyst layer, and the separated water becomes water droplets from the bottom of the decomposition reaction cylinder 2 to the inner bottom of the main body 1. and fall.

なお1分解反応時に上方に拡散する触媒粉は触媒上のフ
ィルタ15を兼ねたガラスウールで補足され、これを通
過した極く微量の触媒粉は分解反応筒2の内面で補足さ
れ1分解反応筒2内に保持留置される。
The catalyst powder that diffuses upward during the 1-decomposition reaction is captured by the glass wool that also serves as a filter 15 on the catalyst, and the extremely small amount of catalyst powder that has passed through this is captured by the inner surface of the decomposition reaction tube 2 and is removed from the 1-decomposition reaction tube. 2.

前述の如く1分解反応時に発生する酸素発生量は前式に
示すように68g(容積で68g/比重1.465=4
6.4cc )という僅かの量から容積比で。
As mentioned above, the amount of oxygen generated during the 1 decomposition reaction is 68g (volume: 68g/specific gravity: 1.465 = 4), as shown in the previous equation.
6.4cc) in terms of volume.

22.400cc/46.4cc=483倍量になる。22.400cc/46.4cc=483 times the amount.

但し。however.

これは0℃、 760m  水銀中の場合の量であり。This is the amount in mercury at 0°C and 760 m.

分解反応時の90℃以上の温度では分解発生した36g
の水は水蒸気となって発生し、酸素の温度も90℃とし
て計算すると。
At a temperature of 90℃ or higher during the decomposition reaction, 36g of decomposition occurred.
Water is generated as water vapor, and the temperature of oxygen is also calculated as 90℃.

となり1滴下した僅かlcc  の過酸化水素から16
00倍量の高温の水蒸気、酸素を発生する。同様に35
%過酸化水素100gの場合は211□0□→ 211
zO+ O□において上式において、少なくとも分解反
応によって発生した水18.53gのみが発生した11
.531の酸素とともに90℃で発生したものとすると
、その容積比は。
16 from just one drop of hydrogen peroxide
Generates 00 times the amount of high temperature water vapor and oxygen. Similarly 35
% For 100g of hydrogen peroxide, 211□0□→211
In the above equation at zO+ O□, only 18.53 g of water was generated due to the decomposition reaction.
.. Assuming that it is generated at 90°C with 531 oxygen, its volume ratio is.

となる、即ち、35%過酸化水素でも容積比は約400
倍である。
That is, even with 35% hydrogen peroxide, the volume ratio is approximately 400.
It's double.

研究当初は触媒を種々の濾過材で小容積の分解反応筒で
発生を試みたが、大容量の発生ガスによる圧力で筒全面
より触媒微粉末を伴って泡状になってガスが噴出し、往
々にして破れて内容物が発生器内に流出落下して液全体
が沸膝状態となり、多量に発生した水蒸気がクーラーで
冷却しきれず、吸入マスク部まで水滴が達する結果とな
り、これらの経験及び化学式に示した容積増より考慮し
、第3図に示すような触媒を収容し得る容積以上の大き
い濾過構造面を有する分解反応筒内に飛散防止フィルタ
で覆った触媒上に、過酸化水素を滴下して触媒を分解反
応筒内に留置せしめ、長期間連続使用し得る分解反応筒
2内明したものである。
At the beginning of the research, attempts were made to generate catalyst in a small-volume decomposition reactor using various filter media, but due to the pressure caused by the large volume of generated gas, bubbles of gas accompanied by fine catalyst powder spewed out from the entire surface of the cylinder. Often, they break and the contents spill out and fall into the generator, causing the entire liquid to boil, and the large amount of water vapor generated cannot be cooled down completely by the cooler, resulting in water droplets reaching the inhalation mask. Considering the increase in volume shown in the chemical formula, hydrogen peroxide is placed on top of the catalyst covered with a scattering prevention filter in the decomposition reaction cylinder, which has a large filtration structure surface larger than the volume that can accommodate the catalyst as shown in Figure 3. This figure shows a decomposition reaction column 2 that can be used continuously for a long period of time by dropping the catalyst and leaving it in the decomposition reaction column.

次いで、この分解反応筒2に過酸化水素を供給する供給
ポンプ3及び過酸化水素瓶4について説明する。
Next, the supply pump 3 and hydrogen peroxide bottle 4 that supply hydrogen peroxide to the decomposition reaction column 2 will be explained.

供給ポンプ3は第1図示の如く内壁面に円形の凹み20
を設け、この凹み20の内周部に沿って耐過酸化水素性
を有する柔軟弾力性のシリコンチューブ21を配し、こ
のチューブ21にはモータ22によって回転する2枚の
円板23の外周部間に少な(とも3ヶ以上1等間隔に回
転自在に取付けた押圧ローラ24が内接し、該押圧ロー
ラ24のしごきによりチューブ21内に過酸化水素を吸
引し、かつ分解反応筒2内に供給できるように構成され
ている。このポンプ3の吸引側は過酸化水素瓶4の首部
25を保持把握した把握手段26の中央に上向きに設置
された吸引針27に連通ずるシリコンチューブと連絡し
ている。
The supply pump 3 has a circular recess 20 on the inner wall surface as shown in the first figure.
A flexible and elastic silicone tube 21 having hydrogen peroxide resistance is disposed along the inner circumference of the recess 20, and the outer circumference of two discs 23 rotated by a motor 22 is attached to the tube 21. Pressure rollers 24 rotatably attached at equal intervals (3 or more) are inscribed in between, and hydrogen peroxide is sucked into the tube 21 by the pressure of the pressure rollers 24, and is supplied into the decomposition reaction tube 2. The suction side of the pump 3 is in communication with a silicone tube that communicates with a suction needle 27 installed upward in the center of a gripping means 26 that holds and grips the neck 25 of the hydrogen peroxide bottle 4. There is.

前記ポンプ3内を通過する過酸化水素はチューブ27内
のみを通る。このポンプ3は一般のポンプのように過酸
化水素がポンプ本体内部に全然触れることなり、シかも
過酸化水素中に分解反応を起こす異物の混入や過酸化水
素によるポンプの損傷の虞れな(、ポンプの回転を中断
したとき押圧ローラ24の少なくとも2個がチューブ2
1を押圧して流れを停止している。従って、一般ポンプ
のようにポンプ停止時にはポンプより上位、下位の管内
の水が落差により流出することなく、チューブ21内に
過酸化水素を保持したまま停止しているので、ポンプの
停止と同時にガスの発生を中断し、再駆動と同時にガス
の発生を可能にするという甚だ効果的なポンプである。
Hydrogen peroxide passing through the pump 3 passes only through the tube 27. With this pump 3, hydrogen peroxide does not come in contact with the inside of the pump body like a general pump, so there is no risk of contamination of foreign matter that causes a decomposition reaction in the hydrogen peroxide or damage to the pump due to hydrogen peroxide ( , when the rotation of the pump is interrupted, at least two of the pressure rollers 24 are pressed against the tube 2.
Press 1 to stop the flow. Therefore, unlike general pumps, when the pump stops, the water in the pipes above and below the pump does not flow out due to the difference in head, and the water stops while retaining the hydrogen peroxide in the tube 21. This pump is extremely effective in that it interrupts the generation of gas and enables the generation of gas at the same time as restarting the pump.

前記過酸化水素瓶4は図に示す如く首部25をやや首長
とするとともに、その口部を封緘したキャップ28はシ
リコンゴム製とし、中央部に前記吸引針27の刺込み部
29と、中央部外の少なくとも一個所には瓶内が正圧、
負圧になったときには気体を通すが、液体を通さない小
さい切れ目を入れた通気孔30を有している。
As shown in the figure, the hydrogen peroxide bottle 4 has a neck 25 with a slightly long neck, and a cap 28 that seals the mouth of the bottle is made of silicone rubber. There is positive pressure inside the bottle in at least one place outside.
It has a vent hole 30 with a small cut that allows gas to pass through when the pressure is negative, but does not allow liquid to pass through.

この通気孔30は貯蔵中、光、温度によって分解発生し
た酸素の逃げ日用となるし、瓶4のキャップ28に吸引
針27を刺し込み、ポンプ3により吸引針27を通して
瓶内の過酸化水素を吸引することにより瓶内が負圧とな
ると空気を瓶4内に入れる役目をする。つまりポンプの
吸引を円滑にする二重の役目をなすものである。
This vent hole 30 is used to escape oxygen decomposed by light and temperature during storage.A suction needle 27 is inserted into the cap 28 of the bottle 4, and the suction needle 27 is passed through the cap 28 of the bottle 4, and the hydrogen peroxide inside the bottle is passed through. When the inside of the bottle becomes negative pressure by suctioning it, it serves to introduce air into the bottle 4. In other words, it plays a dual role of smoothing the suction of the pump.

このことは従来の過酸化水素を発生源とする発生器のよ
うに分解機能の付着の虞れのあるタンクに劇物である過
酸化水素の危険な入れ換え作業を省略できる。また、こ
の瓶4は容器としてのみならず1発生器への供給タンク
の役目を果たすほか、タンクからポンプまでの配管を万
全にして経路を最小限に短くすることができ、かつ触媒
への供給時間を短くし得る容器とタンクを兼ね備えたも
のである。
This makes it possible to omit the dangerous work of replacing hydrogen peroxide, which is a deleterious substance, in a tank, which is likely to be contaminated with decomposition function, as in conventional generators using hydrogen peroxide as a generation source. In addition, this bottle 4 serves not only as a container but also as a supply tank to the generator 1, and also allows the piping from the tank to the pump to be maintained to minimize the shortest route. It combines a container and a tank that can save time.

なお、前記通気孔30の上記役目はメーカーが過酸化水
素の瓶詰めに先立ち洗剤、アルカリ洗浄、酸洗浄、最後
に純水で洗浄して分解の虞れのある油脂、金属イオン、
アルカリ等を完全に除去して安定剤としてリン酸等を加
え酸性にして瓶詰めしても貯蔵中、光、温度によって分
解発生した酸素ガスの逃げ口をなすもので、これにより
瓶の破裂を防ぐものである。
The above-mentioned role of the vent hole 30 is that the manufacturer, before bottling hydrogen peroxide, washes it with detergent, alkaline washing, acid washing, and finally pure water to remove oils and fats that may be decomposed, metal ions, etc.
Even if alkalis, etc. are completely removed and phosphoric acid is added as a stabilizer to make the bottle acidic, it provides an escape port for oxygen gas decomposed due to light and temperature during storage, thereby preventing the bottle from bursting. It is something.

上記の如く発生した多量の高温水蒸気、酸素は本体1よ
り上昇管兼クーラー5内に入る。このクーラー5は第2
図示より明らかな如く、クーラー管32の外周に放射線
状に取付けた放熱板31を有している。垂直のクーラー
管32に入った高温の水蒸気、酸素はその頂部で螺旋状
に降下するクーラー6内に入る。クーラー5及び6の外
側は風導管33で囲い、その下部の冷却ファン9で風導
管33に送風してクーラー5及び6を冷却してガス中の
水蒸気をコンデンスせしめ、水は本体l及び螺旋クーラ
ー6の下に設けた溜枡7に落下せしめる。このように過
大と思われるほどクーラーの容量を大きくしたのは、外
気を強制送風して出てくる酸素を外気温度以下に冷却し
て水滴を含まない酸素を供給管8からマスク部に送気す
るためであり、その理由は過酸化水素による食品の漂白
後の水洗浄不完全による食中毒1例えば、過酸化水素が
口内で発泡9口内炎、喉頭炎を起こした例証を考慮し8
本発生研究初期の分解反応筒が破れ液全体が沸騰状態と
なり、多量の水蒸気が発生した場合、過酸化水素の多量
供給により5N/分以上の酸素の多量発生の場合、その
発生水蒸気のコンデンス液中に微量ではあるが過酸化水
素の存在を検出した経験による安全性と熱い酸素をより
冷たい酸素の吸入の方が爽やかさを惑じることとなるか
らである。
A large amount of high-temperature steam and oxygen generated as described above enters the riser/cooler 5 from the main body 1. This cooler 5 is the second
As is clear from the illustration, a heat sink 31 is provided radially around the outer periphery of the cooler tube 32. The high temperature water vapor and oxygen entering the vertical cooler tube 32 enter the cooler 6 spirally descending at its top. The outside of the coolers 5 and 6 is surrounded by a wind pipe 33, and a cooling fan 9 at the bottom blows air into the wind pipe 33 to cool the coolers 5 and 6 and condense water vapor in the gas, and the water is distributed between the main body l and the spiral cooler. It is made to fall into the reservoir 7 provided below 6. The reason for increasing the capacity of the cooler so much that it seems excessive is to forcefully blow outside air, cool the oxygen that comes out below the outside air temperature, and send the oxygen without water droplets to the mask part from the supply pipe 8. The reason for this is to prevent food poisoning due to incomplete washing with water after bleaching food with hydrogen peroxide.
If the decomposition reactor in the early stage of this generation research ruptures and the entire liquid boils and a large amount of water vapor is generated, if a large amount of oxygen is generated at a rate of 5N/min or more due to the large amount of hydrogen peroxide supplied, the condensed liquid of the generated water vapor may be This is because the experience of detecting the presence of hydrogen peroxide, albeit in a small amount, in the inhalation of hot oxygen leads to confusion about safety and the freshness of inhaling colder oxygen than hot oxygen.

本発生装置は第3図にその一例を示す如く。An example of this generator is shown in FIG.

家庭交流を直流に変換する変換装置34で直流にして抵
抗35を大きい方から小さい方へ順に並べた接点36を
設け、該抵抗35の大きい接点で11/分、2番目に大
きい接点で1.57!/分、五番目の最も抵抗の小さい
接点で31/分の如く発生量を表示して使用者が所望す
る発生量を接点36にダイヤル37の位置により自由に
選択できるようにしている。運の結果1発生量の変更は
勿論1発生の中断、再発生は切換スイッチ38を「断」
、「再投入」で、又患者の容体急変で病院へいくとき、
或いは野外スポーツ等の使用には切換スイッチ38を電
池側39に切換える。
A converter 34 that converts household alternating current into direct current is used to convert the current into direct current. Contacts 36 are provided in which resistances 35 are arranged in order from the largest to the smallest. The contact with the largest resistance 35 has a rate of 11/min, and the contact with the second largest has a rate of 1. 57! The fifth contact with the lowest resistance displays the amount of generation, such as 31/min, so that the user can freely select the desired amount of generation by adjusting the position of the contact 36 and the dial 37. As a result of luck, you can of course change the amount of 1 generation, interrupt 1 generation, or re-occur by turning off the selector switch 38.
, when going to the hospital due to "re-injection" or when the patient's condition suddenly changes,
Alternatively, for use in outdoor sports, etc., the selector switch 38 is switched to the battery side 39.

〔発明の効果〕〔Effect of the invention〕

以上説明した如く1本発明によれば、屋内外での使用は
勿論1本体に過酸化水素収容皿を差し込むだけで即座に
、かつ長時間にわたり酸素を発生させることが可能とな
るとともに1発生量を自由に選択できるなど、各種の優
れた効果を奏するものである。
As explained above, according to the present invention, not only can it be used indoors and outdoors, but also it is possible to generate oxygen instantly and over a long period of time by simply inserting a hydrogen peroxide storage tray into the main body. It has various excellent effects, such as being able to freely select the

【図面の簡単な説明】[Brief explanation of the drawing]

図は本発明の実施例を示すもので、第1図は装置全体の
説明図、第2図は垂直クーラーの斜視図、第3図は分解
反応筒の斜視図、第4図は配線図である。 1・・一本体       2・・・分解反応筒3・・
・ポンプ      4−過酸化水素瓶5・−垂直クー
ラー   6−螺旋クーラー7−溜枡       8
−酸素送気バイブ9−冷却ファン    l〇−水抜き
コック11・・−濾過材     12・−触媒13・
−過酸化水素供給管 14〜分散板     15−・フィルタ材16・−・
フィルタ押えの多孔板 17・・・リム      18−保持体19・−・フ
ィルタ    20−・凹み21−−シリコンチューブ 22−−−−−ポンプ用モータ 23・−円板 24・−押圧クーラー 25−・瓶の首部 26−・−瓶の把握保持装置 27−・吸水針     28−キャップ29・−キャ
ップ面の吸水針刺し込み部30゛−・・通気孔 31・−・クーラーの放熱板 32−クーラー管 33・・−風導管 34・・−直流交換装置  35・−抵抗36−接点 
     37−ダイヤル38−・−切換スイッチ  
39−・−電池第1図 第2図 第3図
The figures show an embodiment of the present invention; Fig. 1 is an explanatory diagram of the entire device, Fig. 2 is a perspective view of the vertical cooler, Fig. 3 is a perspective view of the decomposition reactor, and Fig. 4 is a wiring diagram. be. 1. Main body 2. Decomposition reaction tube 3.
・Pump 4-Hydrogen peroxide bottle 5--Vertical cooler 6-Spiral cooler 7-Sump 8
-Oxygen air supply vibe 9-Cooling fan l〇-Drain cock 11...-Filtering material 12-Catalyst 13-
-Hydrogen peroxide supply pipe 14~distribution plate 15-・filter material 16・-・
Filter holder porous plate 17...Rim 18-Holder 19--Filter 20--Dent 21--Silicon tube 22--Pump motor 23--Disc 24--Press cooler 25-- Bottle neck 26 - Bottle grasping and holding device 27 - Water absorption needle 28 - Cap 29 - Water absorption needle insertion part 30 on the cap surface - Ventilation hole 31 - Cooler heat sink 32 - Cooler tube 33 ...-Wind pipe 34...-DC exchange device 35--Resistor 36--Contact
37-dial 38-・- selector switch
39-・-Battery Figure 1 Figure 2 Figure 3

Claims (9)

【特許請求の範囲】[Claims] (1)過酸化水素を触媒による分解反応によって酸素を
発生せしめる酸素発生装置において、微細な多孔濾過面
を有する耐薬・耐熱性の濾過材よりなる分解反応筒と、
該分解反応筒に収容した粉末触媒に過酸化水素を滴下せ
しめる供給手段と、前記分解反応筒内で発生し、その筒
壁より放散した水蒸気、酸素を冷却するクーラーとを備
えたことを特徴とする酸素発生装置。
(1) In an oxygen generator that generates oxygen through a catalytic decomposition reaction of hydrogen peroxide, a decomposition reaction cylinder made of a chemical-resistant and heat-resistant filter material having a fine porous filtration surface;
It is characterized by comprising a supply means for dropping hydrogen peroxide onto the powder catalyst housed in the decomposition reaction cylinder, and a cooler for cooling water vapor and oxygen generated in the decomposition reaction cylinder and dissipated from the cylinder wall. Oxygen generator.
(2)前記分解反応筒を構成する濾過材が、セラミック
、ガラスフィルタ又は耐過酸化水素及び耐熱性の合成繊
維よりなるフィルタである特許請求の範囲第1項記載の
酸素発生装置。
(2) The oxygen generating device according to claim 1, wherein the filter material constituting the decomposition reaction cylinder is a ceramic filter, a glass filter, or a filter made of hydrogen peroxide-resistant and heat-resistant synthetic fiber.
(3)前記分解反応筒が、触媒収容部上方に大きな空間
が形成できる容積を有するものである特許請求の範囲第
1項記載の酸素発生装置。
(3) The oxygen generating device according to claim 1, wherein the decomposition reaction cylinder has a volume that allows a large space to be formed above the catalyst storage section.
(4)前記分解反応筒の頂部に、過酸化水素供給管を保
持する有孔保持体が嵌合し、該有孔保持体の下面にフィ
ルタ材が固定されている特許請求の範囲第1項乃至第3
項のうちの1項記載の酸素発生装置。
(4) A perforated holder that holds a hydrogen peroxide supply pipe is fitted into the top of the decomposition reaction cylinder, and a filter material is fixed to the lower surface of the perforated holder. to third
The oxygen generator according to item 1 of the items.
(5)前記供給手段が、内壁面に設けた凹みに沿って配
した耐薬性にして柔軟弾力性のチューブをしごくように
接して回転する押圧ローラを備えたポンプと、該ポンプ
の吸引側を過酸化水素瓶に連繋し、出力側を分解反応筒
の頂部を貫通した過酸化水素供給管に連繋したものであ
る特許請求の範囲第1項記載の酸素発生装置。
(5) The supply means includes a pump equipped with a pressure roller that rotates while squeezing a chemically resistant, flexible and elastic tube arranged along a recess provided on the inner wall surface, and a suction side of the pump. The oxygen generating device according to claim 1, which is connected to a hydrogen peroxide bottle and whose output side is connected to a hydrogen peroxide supply pipe passing through the top of a decomposition reaction column.
(6)前記過酸化水素供給管が、その下部末端に分散板
、該分散板の上面側に触媒の上面を覆うフィルタ材、フ
ィルタ材の上面を押える多孔板を備えたものである特許
請求の範囲第1項、第4項及び第5項のうちの1項記載
の酸素発生装置。
(6) The hydrogen peroxide supply pipe is provided with a dispersion plate at its lower end, a filter material covering the upper surface of the catalyst on the upper surface side of the dispersion plate, and a perforated plate pressing the upper surface of the filter material. The oxygen generator according to one of the ranges 1, 4, and 5.
(7)前記ポンプの吸引側に過酸化水素瓶のキャップに
突き刺す吸引針を備え、該吸引針を過酸化水素瓶の首部
を把持する把持装置に上向きに取付けられている特許請
求の範囲第5項記載の酸素発生装置。
(7) The suction side of the pump is provided with a suction needle that pierces the cap of the hydrogen peroxide bottle, and the suction needle is attached upward to a gripping device that grips the neck of the hydrogen peroxide bottle. Oxygen generator as described in section.
(8)前記過酸化水素瓶のキャップが、耐過酸化水素性
の柔軟弾力性のゴム質材で形成され、中央に吸引針の刺
し込み部と、中央部以外の少なくとも一個所に瓶内で発
生した酸素を放出し得る小さい切り口よりなるの通気孔
を設けたものである特許請求の範囲第7項記載の酸素発
生装置。
(8) The cap of the hydrogen peroxide bottle is made of a flexible and elastic rubber material that is resistant to hydrogen peroxide, and has a suction needle insertion part in the center and a cap in at least one place other than the center part inside the bottle. 8. The oxygen generating device according to claim 7, further comprising a vent hole made of a small cut through which the generated oxygen can be released.
(9)前記クーラーが、高温の水蒸気、酸素を通す垂直
管とその上端に連続した螺旋管、又はこれらの管と冷却
ファンとにより構成され、外気温度以下に冷却できるも
のである特許請求の範囲第1項記載の酸素発生装置。
(9) Claims in which the cooler is composed of a vertical pipe that passes high-temperature steam and oxygen and a spiral pipe continuous to the upper end of the vertical pipe, or these pipes and a cooling fan, and can be cooled to below the outside air temperature. The oxygen generating device according to item 1.
JP14163086A 1986-06-18 1986-06-18 Oxygen generator Granted JPS62297201A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP14163086A JPS62297201A (en) 1986-06-18 1986-06-18 Oxygen generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP14163086A JPS62297201A (en) 1986-06-18 1986-06-18 Oxygen generator

Publications (2)

Publication Number Publication Date
JPS62297201A true JPS62297201A (en) 1987-12-24
JPH0428641B2 JPH0428641B2 (en) 1992-05-14

Family

ID=15296506

Family Applications (1)

Application Number Title Priority Date Filing Date
JP14163086A Granted JPS62297201A (en) 1986-06-18 1986-06-18 Oxygen generator

Country Status (1)

Country Link
JP (1) JPS62297201A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050100028A (en) * 2004-04-13 2005-10-18 주식회사 씨앤케이 Oxygen generator
GB2582836A (en) * 2019-04-03 2020-10-07 Oxygenium Ltd Portable system for the production of oxygen

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS492679A (en) * 1972-04-27 1974-01-10

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS492679A (en) * 1972-04-27 1974-01-10

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20050100028A (en) * 2004-04-13 2005-10-18 주식회사 씨앤케이 Oxygen generator
GB2582836A (en) * 2019-04-03 2020-10-07 Oxygenium Ltd Portable system for the production of oxygen
US11383109B2 (en) 2019-04-03 2022-07-12 Oxygenium Ltd. Portable system for the production of oxygen

Also Published As

Publication number Publication date
JPH0428641B2 (en) 1992-05-14

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