CN2367324Y - Simple oxygen-generating device - Google Patents
Simple oxygen-generating device Download PDFInfo
- Publication number
- CN2367324Y CN2367324Y CN 99207034 CN99207034U CN2367324Y CN 2367324 Y CN2367324 Y CN 2367324Y CN 99207034 CN99207034 CN 99207034 CN 99207034 U CN99207034 U CN 99207034U CN 2367324 Y CN2367324 Y CN 2367324Y
- Authority
- CN
- China
- Prior art keywords
- oxygen
- catalytic reaction
- catheter
- reaction tube
- hydrogen peroxide
- 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
Landscapes
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The utility model relates to a simple oxygen-generating device, which is mainly composed of a continuous feeder of hydrogen peroxide solution, a catalytic reaction tube provide with catalyst and a raffinate collector. The simple oxygen-generating device has the oxygen-generating principle that aqueous hydrogen peroxide solution can be used for generating the oxygen through catalytic decomposition. The simple oxygen-generating device has the advantages of simple structure, continuous oxygen generation, controllable process, and convenient utilization and operation, can be widely used for medical first aid, home care and aquiculture using the oxygen, and can be used as chemical experiment demonstration devices in primary and secondary schools, etc.
Description
This utility model relates to a kind of chemical oxygen generation device.
For studying a kind of easy inexpensive chemical oxygen generation device, consulting various countries' patent documentation learns, as JP61-227903[1986], SU15676482[1990], CN8610450.6, CN89106479.6, the disclosed oxygen generator of CN93106953, all there is following defective in the above-mentioned patent of analysis-by-synthesis, the one, system oxygen raw material is difficult to obtain, or oxygen preparation is discontinuous; The 2nd, the residual liquid that generates behind the system oxygen contains the metal waste liquid, discharges easy contaminated environment; The 3rd, the complex structure of oxygen generator is difficult for producing and operation, uses wayward.
For overcoming the deficiency of above-mentioned oxygen generator, the purpose of this utility model provides a kind of oxygen preparation and device is simple, can make pure oxygen continuously, and novel oxygenerator free from environmental pollution.To be applied to medical first aid oxygen, family health care oxygen, aquaculture and transportation occasion with oxygen, also can be as middle and primary schools' chemical experiment demonstration device.
For achieving the above object, technical solution of the present utility model is finished like this: a kind of easy oxygenerator, comprise reinforced feeder, catalytic reaction chamber and tail washings catcher three parts, and the catheter of connection is set by hydrogen peroxide reservoir and bottom, and the control valve that upward disposes, the top catheter that is positioned at control valve is added with the reinforced feeder that the air pressure balance pipe is formed, make the other end of reinforced feeder catheter be connected in an end of the catalytic reaction tube that catalyst is housed, the other end connects the tail washings collecting tank by airway, and reach the tail washings catcher that sidepiece is provided with oxygen exhaustor and tapping valve composition respectively on its cell body, and integral installation is on body.
The catalytic reaction tube that uses in the described oxygenerator, its draw ratio should 〉=3, can decompose fully when guaranteeing hydrogen peroxide by catalytic reaction tube.
Another program of the present utility model is that the reinforced supply mode of pump is set on the catheter of reinforced feeder.
Characteristics of the present utility model are: have reasonable in design, simple in structure, utilize aqueous hydrogen peroxide solution through the oxygenous principle of catalytic decomposition, achieve continuous oxygen generation, process is controlled, use is easy to operate, can be widely used in medical first aid, family health care, aquaculture, and as functions such as middle and primary schools' chemical experiment demonstration devices.
Embodiment is to this novel being further described in conjunction with the accompanying drawings.
Fig. 1 is the oxygenerator structural representation.
Fig. 2 is another embodiment of Fig. 1.
By shown in Figure 1, oxygenerator mainly comprises reinforced feeder, and catalytic reaction tube and tail washings catcher three parts that solid granular catalyst is housed are formed, and integral body is the vertical structure body.It is to adopt hydrogen peroxide storage bottle 1 (groove or jar), and the transparent plastic catheter 3 of connection is set in its bottom, the transparent body is convenient to observe a speed, control valve 4 is housed on the catheter 3, and be positioned at the top of control valve 4 or the pressure of reservoir 1 is the reinforced feeder that normal pressure is formed, make the other end of the catheter 3 that reinforced feeder draws be connected in an end of the catalytic reaction tube 5 that catalyst is housed, the installation site of catalytic reaction tube 5 should be lower than hydrogen peroxide reservoir 1, to keep certain liquid level poor.The airway 6 that the other end of catalytic reaction tube 5 is provided with connection is connected to tail washings collecting tank 7, and on tail washings collecting tank 7 and sidepiece the tail washings catcher that oxygen exhaustor 8 and tapping valve 9 formed is set respectively, the integral installation that makes its combination is on body.
The feeding quantity control valve 4 that is provided with on the catheter 3 that hydrogen peroxide reservoir 1 bottom connects can adopt pin type or electromagnetic switch valve, also can choose the plastic valve of medical control transfusion.The solid granular catalyst that dresses can catalysis hydrogen peroxide (hydrogenperoxide steam generator) decompose in the catalytic reaction tube 5 is as carrier model Ni, Pd, MnO
2Deng, catalyst shape is spherical, cylindrical, this granule should have resistance to water and certain thermostability, guarantees the clarification of life-time service and tail washings.Particle diameter and catalytic reaction tube 5 diameter ratios answer≤1: 5; Catalytic reaction tube 5 draw ratios should 〉=, to guarantee the existing enough permeabilitys of catalytic bed, can not produce channeling again, can decompose when making hydrogen peroxide pass through catalytic reaction tube 5 fully.The volume of catalytic reaction tube 5 is determined by oxygen making amount, generally between 10l-0.005l, because of exothermic catalytic reaction, chooses catalytic reaction tube 5 and should use metal tube or glass tubing.
The tail washings catcher also has the function of gas-liquid separation, oxygen humidification and gas production written instructions except that having the residual liquid of reception, so tail washings collecting tank 7 should select for use transparent resin material or glass to make, so that observe gas production.
See another embodiment shown in Figure 2.Oxygenerator integral body can be the horizontal type structure body.It is to have done corresponding variation on the basis by above-mentioned vertical structure, the feed way of reinforced supply also can be by the pump feed way except that the dropping mode of utilizing liquid level difference, and the catheter 3 that is positioned at the rear side of control valve 4 is provided with reinforced control pump 10, control pump 10 can be chosen micro centrifugal pump, peristaltic pump or magnetic drive pump, the amount of infusion of pump can be fixed, also can be adjustable, generally between 10 (l/min)-0.01 (l/min).Adopt the installation site between this kind mode oxygenerator each several part not limited by liquid level, be particularly suitable for the big occasion of oxygen consuming amount, as used for aquiculture oxygen, the big I of hopper is determined by oxygen consuming amount, generally between 50l-0.05l.
The employed hydrogen peroxide of oxygen preparation can be common industrial hydrogen peroxide, and its concentration can be chosen wantonly between 50%-5%.
For ease of the oxygen preparation of this device is described, existing illustrative example is as follows:
Embodiment one
Adopt the 200ml reservoir, add 27.5% industrial hydrogen peroxide raw material, 5g ball-type φ 1-2mmMnO packs in the catalytic reaction tube of φ 10 * 2 * 100mm
2/ hour catalyst, in catalytic reaction tube, splash into hydrogen peroxide with 50-100ml/ hour speed, hydrogen peroxide is decomposed in catalytic reaction tube generate water and oxygen, can be with the speed of oxygen supply oxygen supply of 150ml/min 2-3 hour, gas production can be by the control of the adjusting control valve on the catheter, and the oxygen of generation reaches more than 99.5% by analysis, and tail washings is as clear as crystal, free from environmental pollution, and this catalytic reactor can prolonged and repeatedly use.
Embodiment two
Adopt the oxygenerator of Fig. 2, by the hydrogen peroxide raw material of reservoir adding 27.5% or 15%, MnO packs in the metal catalysed reaction pipe of φ 76 * 300mm
2/ waterglass ball-type (φ 2-3mm) catalyst or φ 3-4mmPdL
2O
3Catalyst 1100g imports hydrogen peroxide solution continuously by peristaltic pump in catalytic reaction tube, the result can obtain the pure oxygen of 10-17l/min, and this oxygen can be used for medical treatment or used for aquiculture oxygen.
Claims (3)
1, a kind of easy oxygenerator, comprise reinforced feeder, catalytic reaction chamber and tail washings catcher three parts, it is characterized in that it has adopts hydrogen peroxide reservoir (1) and bottom that the catheter (3) of connection is set, and the control valve (4) that upward disposes, the top catheter (3) that is positioned at control valve (4) is added with the reinforced feeder that air pressure balance pipe (2) is formed, make the other end of reinforced feeder catheter (3) be connected in an end of the catalytic reaction tube (5) that catalyst is housed, the other end connects tail washings collecting tank (7) by airway (6), and reach the tail washings catcher that sidepiece is provided with oxygen exhaustor (8) and tapping valve (9) composition respectively on its cell body, and integral installation is on body.
2,, it is characterized in that the draw ratio of described catalytic reaction tube (5) answers 〉=3 by the described a kind of easy oxygenerator of claim 1.
3, by the described a kind of easy oxygenerator of claim 1, the feed way that it is characterized in that described reinforced feeder can be a dropping mode of utilizing liquid level difference, also can be pump (10) feed way is set on catheter (3).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99207034 CN2367324Y (en) | 1999-03-26 | 1999-03-26 | Simple oxygen-generating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN 99207034 CN2367324Y (en) | 1999-03-26 | 1999-03-26 | Simple oxygen-generating device |
Publications (1)
Publication Number | Publication Date |
---|---|
CN2367324Y true CN2367324Y (en) | 2000-03-08 |
Family
ID=34001145
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN 99207034 Expired - Fee Related CN2367324Y (en) | 1999-03-26 | 1999-03-26 | Simple oxygen-generating device |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN2367324Y (en) |
-
1999
- 1999-03-26 CN CN 99207034 patent/CN2367324Y/en not_active Expired - Fee Related
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN101555455A (en) | Culture/harvesting method of microalgae and system | |
CN202017009U (en) | Denitrification type methane anaerobic oxidized bacterium enriching system based on automatic control | |
CN1986453A (en) | UASB biological pneumatic circulation stirring technique | |
CN106219691A (en) | A kind of ozonated water generator | |
CN108821498A (en) | A method of black and odorous water is handled using bionics method | |
CN2367324Y (en) | Simple oxygen-generating device | |
CN101275233A (en) | Hydrogen production method using alcohol as raw material | |
CN202643427U (en) | Separating type anaerobic baffled reactor (ABR) | |
CN102451607A (en) | Internal and external dual-circulation reaction method and device for absorbing hydrogen sulfide | |
CN110183029A (en) | A kind of apparatus and method converting organic wastewater to acetic acid | |
CN206156811U (en) | Ozone water generator | |
CN1272441C (en) | High-efficiency microorganism hydrogen preparation and hydrogen energy-electric energy conversion integrating apparatus | |
CN214571988U (en) | Device for synchronously enriching acidic and alkaline DAMO microorganisms | |
CN110656027A (en) | Gas-liquid reverse transmission biomembrane reactor for preparing ethanol by fermenting waste gas CO/CO2 | |
CN2923713Y (en) | Pressure-type self-circulating self-feeding biological methane generating device | |
CN102389707B (en) | Automatic control-based paddle drop-type gas-holding internal-cycle denitrification anaerobic methane oxidation reactor | |
CN113980781A (en) | Tidal carbon dioxide biological methanation device and method | |
CN208776380U (en) | For ozone or the experimental provision of hydrogen peroxide oxidation sewage | |
CN208603962U (en) | A kind of sewage disposal system under the conditions of the cold and oxygen deficient suitable for highlands | |
CN201593003U (en) | PBF filter filler | |
CN107416976A (en) | A kind of synchronous methane phase and the processing method of elemental sulfur device and sulfur-bearing organic liquid waste | |
CN206089832U (en) | Electrolysis water tank and use domestic ozone water generator of this electrolysis water tank | |
CN204848425U (en) | Simple and easy membrane bioreactor | |
CN216192231U (en) | Tidal carbon dioxide biological methanation device | |
CN107815447A (en) | A kind of compound algae microballoon of immobilization and its application |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
C19 | Lapse of patent right due to non-payment of the annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
MM1K | Cease caused by non payment of annual fee |