CN105752935B - Ball-type floating warehouse formula device for producing oxygen from chemical substance - Google Patents
Ball-type floating warehouse formula device for producing oxygen from chemical substance Download PDFInfo
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- CN105752935B CN105752935B CN201610234953.3A CN201610234953A CN105752935B CN 105752935 B CN105752935 B CN 105752935B CN 201610234953 A CN201610234953 A CN 201610234953A CN 105752935 B CN105752935 B CN 105752935B
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- warehouse
- ball
- oxygen
- floating
- reaction warehouse
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B13/00—Oxygen; Ozone; Oxides or hydroxides in general
- C01B13/02—Preparation of oxygen
- C01B13/0203—Preparation of oxygen from inorganic compounds
- C01B13/0211—Peroxy compounds
- C01B13/0214—Hydrogen peroxide
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- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
The invention discloses a kind of ball-type floating warehouse formula device for producing oxygen from chemical substance, oxygen is produced using catalyst decomposing hydrogen dioxide solution, by hollow out ball-type pedestal, floating warehouse, reaction warehouse, flexible oxygen cathete, hydrogen peroxide locker room, goes out the part such as oxygen control valve and bidirectional decompression valve and constitutes.It is characterized in that：Floating warehouse uses closed bivalve hollow structure, and is integrated with reaction warehouse, floating warehouse and reaction warehouse is always positioned above pedestal by buoyancy, and hydrogen peroxide enters reaction warehouse from below all the time；By the ball-type pedestal and reaction warehouse inner casing of hollow out, enable floating warehouse and reaction warehouse all-direction rotation, hydrogen peroxide can free in and out reaction warehouse；By controlling the contact of hydrogen peroxide and catalyst in reaction warehouse, to control the generation of oxygen；By controlling the air pressure of reaction warehouse, to control hydrogen peroxide to pass in and out reaction warehouse；Pressure is maintained by bidirectional control valve in zone of reasonableness, to ensure safety.The present invention can make production oxygen device volume compact, use easy to carry, the stable abundance of aerogenesis.
Description
Technical field
The present invention relates to chemical oxygen generation field, especially a kind of utilization hydrogen peroxide prepares the device for producing oxygen from chemical substance of oxygen.
Background technology
Encounter in daily life in medical treatment and often and need the situation of oxygen uptake, situation can be very critical sometimes, promptly
Quick oxygen uptake often saves a life or wins the quality time to save life.Inhalation device common at present has following
It is several：1st, high-pressure cylinder, shortcoming is：Such device is relatively cumbersome, and pressure is high, and special decompressor is needed when using, with rising
Come dangerous big, it is also inconvenient.2nd, Medical oxygen bag, shortcoming is：Space-consuming is larger, and oxygen is easily revealed, inconvenient to carry.
3rd, the small size oxygen cylinder of common market sale, shortcoming is：Oxygen storage capacity is small, it is impossible to which continuous oxygen supply, using effect is not good enough.4th, market
The oxygen of sale is vertical must to wait chemical oxygen generator, and shortcoming is：Volume is larger, relatively cumbersome, inconvenient to carry, and complex operation, takes
When it is laborious, produce that amount of oxygen is small, alkaline reaction product can cause the pollution of environment.5th, using the oxygenerator system of sieve technology
Oxygen, and electrochemical method oxygen, shortcoming are：Continuing power supply ability oxygen supply is all had to rely on, and volume is larger, takes
With height, it is impossible to carry with.
After the research to above-mentioned common inhalation device, the inventors found that：Lack one kind in the market to take
Band and easy to use, compact, without supply of electric power, oxygen purity is high and oxygen-producing amount is big, can continue oxygen supply, can be at any time
Open and close, the Portable oxygen-generating device of final product cleanliness without any pollution.
The content of the invention
In order to overcome the above-mentioned deficiencies of the prior art, the invention provides a kind of ball-type floating warehouse formula device for producing oxygen from chemical substance.
The technical solution adopted in the present invention is：Oxygen is produced using catalyst decomposing hydrogen dioxide solution, by hollow out ball-type
Pedestal, floating warehouse, reaction warehouse, flexible oxygen cathete, hydrogen peroxide locker room, go out the part such as oxygen control valve and bidirectional decompression valve composition.Its
It is characterised by：Floating warehouse uses closed bivalve hollow structure, and is integrated with reaction warehouse, makes floating warehouse and anti-by buoyancy
Storehouse is answered to be always positioned above pedestal, hydrogen peroxide enters reaction warehouse from below all the time；By in the ball-type pedestal and reaction warehouse of hollow out
Shell, enables floating warehouse and reaction warehouse all-direction rotation, and hydrogen peroxide can free in and out reaction warehouse；By controlling hydrogen peroxide and reaction warehouse
The contact of interior catalyst, to control the generation of oxygen；By controlling the air pressure of reaction warehouse, to control hydrogen peroxide to pass in and out reaction warehouse；
Pressure is maintained by bidirectional control valve in zone of reasonableness, to ensure safety.
Above-mentioned technical proposal can be seen that：Compared with prior art, compact conformation of the present invention, compact, are convenient for carrying,
Oxygen-producing amount is big, and aerogenesis is continual and steady, can long period continuous oxygen supply；Simple to operate, process control can start and stop at any time
Only；Oxygen purity is high, complies fully with medical oxygen standard；Final product be oxygen and water, it is environmentally safe.
Brief description of the drawings
Technical scheme in order to illustrate the embodiments of the present invention more clearly, makes required in being described below to embodiment
Accompanying drawing is briefly described, it should be apparent that, drawings in the following description are only some embodiments of the present invention, for
For those of ordinary skill in the art, on the premise of not paying creative work, it can also obtain other according to these accompanying drawings
Accompanying drawing.
Fig. 1 ball-type floating warehouse formula device for producing oxygen from chemical substance overall schematics of the present invention
1 in figure, oxygen interface tube 2, knob 3, filtering and humidifying layer 4, bidirectional decompression valve
5th, hydrogen peroxide locker room 6, catalyst 7, reaction warehouse 8, hollow out ball-type pedestal
9th, base seat support 10, go out oxygen control valve 11, galenic 12, flexible oxygen cathete
13rd, floating warehouse shell 14, floating warehouse 15, floating warehouse inner casing and reaction warehouse shell
16th, hollow type reaction warehouse inner casing
Fig. 2, floating warehouse and reaction warehouse schematic diagram
1st, floating warehouse oxygen exhaust 2, floating warehouse shell 3, floating warehouse 4, floating warehouse inner casing and reaction warehouse shell
5th, mouth under the hollow type reaction warehouse inner casing 7 of catalyst 6, hollow out ball-type pedestal 8, floating warehouse and reaction warehouse
9th, base seat support 10, bottom of bottle fixed part 11, reaction warehouse oxygen exhaust 12, reaction warehouse
Fig. 3 hollow out ball-type pedestal schematic diagrames
1 in figure, hollow out ball-type pedestal sphere 2, hollow out ball-type pedestal suitable for reading 3, hollow out support
4th, cut-out openings 5, base seat support endoporus 6, base seat support and ball-type pedestal connecting portion
Embodiment
Below in conjunction with the accompanying drawing in the embodiment of the present invention, the technical scheme in the embodiment of the present invention is carried out clear, complete
Site preparation is described, it is clear that described embodiment is only a part of embodiment of the invention, rather than whole embodiments.It is based on
Embodiment in the present invention, it is all other that those of ordinary skill in the art are obtained under the premise of creative work is not made
Embodiment, belongs to the scope of protection of the invention.
Floating warehouse shell (structure 2 of accompanying drawing 2) constitutes closed hollow structure formation floating warehouse with floating warehouse inner casing (structure 4 of accompanying drawing 2)
(structure 3 of accompanying drawing 2), produces buoyancy, by controlling the size of floating warehouse (structure 3 of accompanying drawing 2), to control the size of buoyancy, it is ensured that floating
(both use integral structure, and floating warehouse inner casing is total to reaction warehouse shell for storehouse (structure 3 of accompanying drawing 2) and reaction warehouse (structure 12 of accompanying drawing 2)
With same structure, to strengthen fastness and reduce volume) top that is always positioned at hollow out ball-type pedestal (structure 7 of accompanying drawing 2) is (floating
The relation in storehouse, reaction warehouse and hollow out ball-type pedestal is that the position of floating warehouse centre of buoyancy is higher than the position of floating warehouse and the center of gravity of reative cell, and
Higher than the position of the hollow out ball-type pedestal centre of sphere).Hollow type reaction warehouse inwall (structure 6 of accompanying drawing 2) uses hollow out ball shape gear, internal diameter
Mouth (structure 8 of accompanying drawing 2) internal diameter, which is less than, under micro- external diameter more than hollow out ball-type pedestal (structure 7 of accompanying drawing 2), floating warehouse and reaction warehouse engraves
The external diameter of empty ball-type pedestal (structure 7 of accompanying drawing 2), to ensure that floating warehouse (structure 3 of accompanying drawing 2) and reaction warehouse (structure 12 of accompanying drawing 2) will not
Depart from hollow out ball-type pedestal (structure 7 of accompanying drawing 2), and can freely rotate, while hydrogen peroxide can free in and out reaction warehouse.Reaction warehouse
(structure 12 of accompanying drawing 2) positioned at reaction warehouse periphery and top, is designed to from the bottom to top progressively built with catalyst (structure 5 of accompanying drawing 2)
Increase, and to be porous cellular, is easy to control the catalysis of hydrogen peroxide and passing through for liquid and gas.Catalyst (the knot of accompanying drawing 2
Structure 5) root edge plane is higher than mouth (structure 8 of accompanying drawing 2) plane under floating warehouse and reaction warehouse, and its space is as cushion space.Hollow out ball-type
Can partly it be removed at the top of pedestal (structure 7 of accompanying drawing 2) ball-type, to save material and be beneficial to the turnover of hydrogen peroxide, ball wall thickness can be adopted
With the mode from top to bottom progressively thickened, to increase fastness, and mitigate weight, facilitate hydrogen peroxide to pass in and out, and beneficial to floating warehouse and
Reaction warehouse surrounds hollow out ball-type pedestal all-direction rotation.Flexible oxygen cathete (structure 12 of accompanying drawing 1) is sufficiently flexible, and keeps enough
Patency, to ensure that it is freely defeated that floating warehouse (structure 3 of accompanying drawing 2) and reaction warehouse (structure 12 of accompanying drawing 2) can freely rotate oxygen energy simultaneously
Go out.
When device is closed, go out oxygen control valve (structure 10 of accompanying drawing 1) closing, it is galenic (structure 11 of accompanying drawing 1), soft
Property oxygen cathete (structure 12 of accompanying drawing 1), floating warehouse (structure 14 of accompanying drawing 1), reaction warehouse (structure 7 of accompanying drawing 1) and hollow out ball-type pedestal (accompanying drawing
1 structure 8) part form a confined space, due to gas pressure intensity effect, hydrogen peroxide can not enter the reaction warehouse (structure of accompanying drawing 1
7) catalyst (structure 6 of accompanying drawing 1), is not reached, the just generation without oxygen yet.Now, if whole device run-off the straight or
Lodging, due to buoyancy effect all the time straight up, in the presence of buoyancy, floating warehouse (structure 14 of accompanying drawing 1) and reaction warehouse (accompanying drawing
1 structure 7) it can be rotated around the bulb of hollow out ball-type pedestal (structure 8 of accompanying drawing 1), and ensure position all the time up, hydrogen peroxide is still
It is old to enter reaction warehouse (structure 7 of accompanying drawing 1), catalyst (structure 6 of accompanying drawing 1) is not reached, still no oxygen is produced.Control double
Volume of a container shared by oxygen water, even if whole device is inverted, still ensures that safety.
During opening device, turn knob (structure 2 of accompanying drawing 1) opens out oxygen control valve (structure 10 of accompanying drawing 1), reaction warehouse is (attached
Fig. 1 structures 7) reduction of interior air pressure, the hydrogen peroxide in hydrogen peroxide locker room (structure 5 of accompanying drawing 1) passes through in the presence of liquid pressure
Cut-out openings (structure 4 of accompanying drawing 3), base seat support endoporus (structure 5 of accompanying drawing 3) and the hollow type reaction warehouse inner casing of hollow out ball-type pedestal
(structure 6 of accompanying drawing 2) enters reaction warehouse (structure 7 of accompanying drawing 1) contact catalyst (structure 6 of accompanying drawing 1), and hydrogen peroxide is decomposed reaction,
Produce oxygen.
The hydrogen peroxide concentration for having just enter into reaction warehouse (structure 7 of accompanying drawing 1) is high, and what is contacted first is catalyst (structure 6 of accompanying drawing 1)
Bottom, catalytic amount is few herein, can prevent that originally catalytic reaction is excessively fierce.With the progress of reaction, hydrogenperoxide steam generator
Concentration is gradually reduced, and the pressure that oxygen is produced is relatively low, and dioxygen water level will gradually rise, and gradually increase with catalyst exposure,
Catalytic capability also progressively strengthens, and oxygen-producing amount also increases；If the pressure pressure produced is higher, compressing liquid level, makes dioxygen downwards
Contact of the water with catalyst is reduced, and oxygen-producing amount is also reduced, so repeatedly until the oxygen pressure produced reaches again with liquid pressure
To balance, it is ensured that production oxygen speed remains stable.
React the oxygen produced and enter floating warehouse (structure 3 of accompanying drawing 2) via reaction warehouse oxygen exhaust (structure 11 of accompanying drawing 2) upwards,
Flexible oxygen cathete (structure 12 of accompanying drawing 1) is entered subsequently into the galenic (structure of accompanying drawing 1 by floating warehouse oxygen exhaust (structure 1 of accompanying drawing 2) again
11), by filtering and wetting layer (structure 3 of accompanying drawing 1), go to eliminate the unusual smell and impurity, and appropriate humidifying, through the oxygen interface tube (knot of accompanying drawing 1
Structure 1) output.The size for controlling out oxygen control valve (structure 10 of accompanying drawing 1) to be open, the change with regard to reaction warehouse air pressure can be controlled, so that
Contact of the hydrogen peroxide with catalyst is controlled, and then controls the process of whole decomposition reaction.During production oxygen, if whole device
Run-off the straight or lodging, in the presence of buoyancy, floating warehouse (structure 14 of accompanying drawing 1) and reaction warehouse (structure 7 of accompanying drawing 1) can be around hollow outs
The bulb of ball-type pedestal (structure 8 of accompanying drawing 1) is rotated, and ensures position all the time up, and hydrogen peroxide still can enter anti-from following
Storehouse (structure 7 of accompanying drawing 1) is answered, the oxygen of generation remains to normal output, the progress for making production oxygen reaction energy safe and orderly.And entirely fill
Putting can freely change between above-mentioned unlatching and closed mode.
With the progress of reaction, hydrogenperoxide steam generator volume is gradually decreased, and bidirectional control valve (structure 4 of accompanying drawing 1) is inwardly opened
Open, ambient atmos enter hydrogen peroxide locker room (structure 5 of accompanying drawing 1), what supplement hydrogenperoxide steam generator was reduced because producing chemical reaction
Volume；In special status, when device pressure is significantly raised, bidirectional control valve (structure 4 of accompanying drawing 1) is outwards opened, and reduces dioxygen
The pressure of water locker room (structure 5 of accompanying drawing 1), maintains device in a safe condition.
The principle and embodiment of the ball-type floating warehouse formula device for producing oxygen from chemical substance provided above the embodiment of the present invention are carried out
Illustrate, the explanation of above example is only intended to help to understand method and its core concept of the invention；Simultaneously for ability
The those skilled in the art in domain, according to the thought of the present invention, will change in specific embodiments and applications, comprehensive
Upper described, this specification content should not be construed as limiting the invention.
Claims (9)
1. a kind of ball-type floating warehouse formula device for producing oxygen from chemical substance, produces oxygen, by hollow out ball-type using catalyst decomposing hydrogen dioxide solution
Pedestal, floating warehouse, reaction warehouse, flexible oxygen cathete, hydrogen peroxide locker room, go out oxygen control valve and bidirectional decompression valve group into its feature exists
In：Floating warehouse uses closed bivalve hollow structure, and is integrated with reaction warehouse, floating warehouse and reaction warehouse is begun by buoyancy
Final position is above pedestal, and hydrogen peroxide enters reaction warehouse from below all the time；By the ball-type pedestal and reaction warehouse inner casing of hollow out, make to float
Storehouse and reaction warehouse can all-direction rotation, hydrogen peroxide can free in and out reaction warehouse；By controlling hydrogen peroxide with being catalyzed in reaction warehouse
The contact of agent, to control the generation of oxygen；By controlling the air pressure of reaction warehouse, to control hydrogen peroxide to pass in and out reaction warehouse；By double
Pressure is maintained to control valve in zone of reasonableness, to ensure safety.
2. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Floating warehouse uses one with reaction warehouse
Body formula structure, floating warehouse inner casing unites two into one with reaction warehouse shell, to strengthen fastness and reduce volume.
3. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Floating warehouse uses closed bivalve
Hollow structure, both ensures to provide enough buoyancy, again disengaging beneficial to oxygen；Reaction warehouse inwall uses hollow out ball shape structure, both sharp
Reaction warehouse is passed in and out in hydrogen peroxide, floating warehouse and reaction warehouse are beneficial to again and is rotated around hollow out ball-type pedestal.
4. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Pedestal uses hollow out ball-type,
Facilitate hydrogen peroxide to pass in and out, and hollow out ball-type pedestal all-direction rotation is surrounded beneficial to floating warehouse and reaction warehouse.
5. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Floating warehouse, reative cell and hollow out
The relation of ball-type pedestal is that the position of floating warehouse centre of buoyancy is higher than the position of floating warehouse and the center of gravity of reative cell, and higher than hollow out ball-type base
The position of the seat centre of sphere.
6. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Catalyst is located at reaction warehouse week
Side and top, are designed to be stepped up from the bottom to top, and to be porous cellular, are easy to control catalysis and the liquid of hydrogen peroxide
And gas passes through；And plane where catalyst root edge is higher than plane where mouth under floating warehouse and reaction warehouse.
7. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Adjusted using bidirectional decompression valve
Pressure is saved, hydrogen peroxide is stored chamber pressure and is in zone of reasonableness.
8. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Used between floating warehouse and galenic
The connection of flexible oxygen cathete, did not only influence floating warehouse and reaction warehouse around the rotation of hollow out ball-type pedestal again beneficial to conveying oxygen.
9. ball-type floating warehouse formula device for producing oxygen from chemical substance according to claim 1, it is characterised in that：Saliva under floating warehouse and reaction warehouse
Flat internal diameter is less than ball-type pedestal external diameter and place plane is less than plane where the pedestal centre of sphere, and simultaneous reactions storehouse internal diameter is micro- to be more than ball
Type pedestal external diameter, had both ensured that reaction warehouse and floating warehouse can be rotated freely around pedestal, again will not be with base-separation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610234953.3A CN105752935B (en) | 2016-04-15 | 2016-04-15 | Ball-type floating warehouse formula device for producing oxygen from chemical substance |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610234953.3A CN105752935B (en) | 2016-04-15 | 2016-04-15 | Ball-type floating warehouse formula device for producing oxygen from chemical substance |
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| Publication Number | Publication Date |
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| CN105752935A CN105752935A (en) | 2016-07-13 |
| CN105752935B true CN105752935B (en) | 2017-10-27 |
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| Application Number | Title | Priority Date | Filing Date |
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| CN201610234953.3A Active CN105752935B (en) | 2016-04-15 | 2016-04-15 | Ball-type floating warehouse formula device for producing oxygen from chemical substance |
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Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105236356B (en) * | 2015-09-14 | 2017-09-15 | 高荣帅 | Portable integral controllable chemical oxygenerator |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2152574Y (en) * | 1993-03-12 | 1994-01-12 | 李英 | Simple adjustable steady-flow oxygen generator |
| CN2193176Y (en) * | 1994-01-06 | 1995-03-29 | 俞文国 | Chemical oxygen producing apparatus for vehicle and ship |
| CN101687158A (en) * | 2007-07-06 | 2010-03-31 | 三菱铅笔株式会社 | Gas generation apparatus |
| CN105236356A (en) * | 2015-09-14 | 2016-01-13 | 高荣帅 | Portable integrated controllable chemical oxygen production apparatus |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP3682316B2 (en) * | 1995-03-10 | 2005-08-10 | ビーゴ株式会社 | Oxygen generator |
-
2016
- 2016-04-15 CN CN201610234953.3A patent/CN105752935B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2152574Y (en) * | 1993-03-12 | 1994-01-12 | 李英 | Simple adjustable steady-flow oxygen generator |
| CN2193176Y (en) * | 1994-01-06 | 1995-03-29 | 俞文国 | Chemical oxygen producing apparatus for vehicle and ship |
| CN101687158A (en) * | 2007-07-06 | 2010-03-31 | 三菱铅笔株式会社 | Gas generation apparatus |
| CN105236356A (en) * | 2015-09-14 | 2016-01-13 | 高荣帅 | Portable integrated controllable chemical oxygen production apparatus |
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