CN206970719U - Field plate - Google Patents
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- CN206970719U CN206970719U CN201720348293.1U CN201720348293U CN206970719U CN 206970719 U CN206970719 U CN 206970719U CN 201720348293 U CN201720348293 U CN 201720348293U CN 206970719 U CN206970719 U CN 206970719U
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- water
- hydrogen
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- pure water
- oxygen
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E60/00—Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
- Y02E60/30—Hydrogen technology
- Y02E60/36—Hydrogen production from non-carbon containing sources, e.g. by water electrolysis
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- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model provides a kind of field plate, it is mainly included by power supply unit, control board, touch control display interface, hydrogen-oxygen water electrolyzer, pure water storage tank, ion exchange resin filter core, flow control valve, the component such as aqueous accumulator tank and macromolecule gas-water separation component forms, it utilizes control board and touch control display interface control power supply and pure water input supply hydrogen-oxygen water electrolyzer, caused water and oxygen and water are exported with hydrogen after water electrolysis, the water that wherein exports and hydrogen are by macromolecule gas-water separation component by water and Hydrogen Separation, make hydrogen output for using, and aqueous is back to aqueous accumulator tank and leads to pure water storage tank for recycling, also same but oxygen is expelled directly out oxygen water, obtain according to this reduce pipeline and produce aqueous vapor resistance when preventing that aqueous from flowing by pumping pressurization simplify structure and the good field plate of efficiency.
Description
Technical field
The utility model about a kind of field plate, its can by after water electrolysis by caused water and oxygen and water and hydrogen
Output, water and hydrogen and by macromolecule gas-water separation component by water and Hydrogen Separation, make hydrogen output for use, and aqueous is through electricity
Control is back to aqueous accumulator tank and leads to pure water storage tank for recycling, and obtains according to this and reduces pipeline and prevent water by pumping pressurization
Aqueous vapor resistance is produced when liquid stream is dynamic and simplifies structure and the good field plate of efficiency.
Background technology
Hydrogen (Hydrogen) is a kind of colourless, odorless, tasteless, nontoxic imflammable gas, is also most basic chemistry
Element and raw material, for many years hydrogen applied by substantial amounts of in chemistry i.e. biotechnology processing procedure, its related manufacture, storage,
Transport and substantially construction is complete with criterion.
The generation and application of hydrogen energy source, hydrogen in recent years, because of the row's of having no carbon in the manufacture circulation of hydrogen-oxygen body separation oxyhydrogen
Problem, thus turned into the green energy of most popular research exploitation in recent years and emerging product.
The production method of wherein hydrogen is broadly divided into two major classes, and one kind is to be catalyzed production hydrogen manufacturing oxygen side by chemical raw material
Method, it includes steam recombination method (Steam Reforming), partial oxidation process (Partial Oxidation), water-gas method
(Coal Gasification)；It is another kind of, hydrogen manufacturing oxygen method is produced for non-chemical breaking of raw material, it includes water electrolysis method
(Water Splitting by Electrolysis), water photoelectricity solution (Photo Electrochemical Water
Splitting a small amount of silicol process etc.) and in laboratory.
At present oxyhydrogen caused by water electrolysis method, is mainly used on energy battery, such as car engine burns what is used
Power source, it belongs to hydrogen-oxygen interflow use state.
Traditional water electrolysis method is produced in hydrogen-oxygen gas method again, and its water intake mode system is with physics high-low water level difference principle, therefore
It is relatively limited to produce hydrogen-oxygen amount.
Look forward to the future, hydrogen while will be produced needed for human breathing by reduction decomposition water outlet in various hydrogen production process
Oxygen, it is believed that following hydrogen energy era will be an environmental protection and economy complementary generation.
By being learnt in experiment, hydrogen H2 category activated gas, if collected in atmospheric environment storage concentration more than 4%~
High temperature is met again in the range of 95% (less than 4%, more than 95% category safety) or flare is possible to ignite, as U.S. FDA confirms
99.999% High Purity Hydrogen enter human body after, form a kind of physiological inert gas on the contrary, it is not only harmless on the contrary can be human body
High oxidation free radical discarded object caused by burning glucose is reduced to water, and pure hydrogen is entering alternative anti-ization of human body and excluded
Bad free radical, it is seen that hydrogen is not pernicious gas to human body under certain situation.
But how to design the field plate that structure is simplified and efficiency is good is an important topic, studies and send out through inventor
Existing water electrolysis method is a kind of more simple generation hydrogen method of i.e. production i.e., and as known, hydrogen-oxygen water electrolyzer makes hydrone exist
Negative electrode is reduced generation hydrogen, and hydrone is oxidized in anode and produces oxygen, this really a kind of simple clean generation hydrogen
Good method.
The content of the invention
According to upper principle, inventor, which researches and develops, completes the utility model field plate, and it is mainly included by power supply unit, control
Circuit board processed, touch control display interface, hydrogen-oxygen water electrolyzer, pure water storage tank, ion exchange resin filter core, flow control valve, aqueous recovery
Groove and macromolecule gas-water separation component etc. form.
The utility model provides a kind of field plate, and it includes a power supply unit, a control board, a touch-control
Display interface, a hydrogen-oxygen water electrolyzer, a pure water storage tank, an ion exchange resin filter core, flow control valve, an aqueous accumulator tank and
One macromolecule gas-water separation component；
The power supply unit, for the power input of the field plate, it is connected to control board；
The control board, it is electrically connected with provided with control circuit and with touch control display interface and hydrogen-oxygen water electrolyzer；
The touch control display interface, it is the interface of the control circuit communication of operator and control board；
The hydrogen-oxygen water electrolyzer, its cathode terminal are provided with a water and oxygen output tube and are connected to pure water storage tank and anode tap
Provided with a water and hydrogen efferent duct and aqueous accumulator tank is connected to, water through aqueous accumulator tank and is connected to water with hydrogen efferent duct
The hydrogen delivery outlet set above liquid accumulator tank；
The pure water storage tank, its upper end are provided with pure water hand-hole and oxygen tap, storage tank and are provided with pure water liquid level sensor,
Above-mentioned pure water hand-hole, injection end is supplied for pure water source, the pure water storage tank bottom side is provided with an input pipe, and the input pipe other end connects
Hydrogen-oxygen water electrolyzer is connected to, the input pipe is provided with water filling pumping between pure water storage tank and hydrogen-oxygen water electrolyzer, makes in pure water storage tank
The pressurized injection hydrogen-oxygen water electrolyzer of pure water in carry out water electrolysis effect, above-mentioned pure water liquid level sensor and water filling pumping are electrical
Control board is connected to, for controlling the input of pure water and starting or stoping for water filling pumping；
The ion exchange resin filter core, on above-mentioned input pipe, there is provided the pure water of filtering input hydrogen-oxygen water electrolyzer, to promote
The purity of pure water simultaneously improves electrolysis effectiveness；
The flow control valve, between the input pipe of hydrogen-oxygen water electrolyzer front end, flow control valve is electrically connected to control for it
The pure water input quantity of circuit board processed, according to this control input pipe, make to reach optimal water electrolysis efficiency；
The aqueous accumulator tank, its upper end are provided with hydrogen delivery outlet, are provided with recycle-water liquid level sensor, above-mentioned water in accumulator tank
Liquid accumulator tank, the aqueous accumulator tank of the aqueous recycling of hydrogen and water is produced for the reduction of hydrogen-oxygen water electrolyzer electrolyzing pure water, should
Pure water storage tank bottom side is provided with a return duct, and the return duct other end is connected to pure water storage tank, the return duct in aqueous accumulator tank with it is pure
Backflow pumping is provided between water storage tank, makes the withdrawal water in aqueous accumulator tank is pressurized to be back to pure water storage tank, above-mentioned aqueous recovery
Recycle-water liquid level sensor in groove and backflow pumping are electrically connected to control board, for control backflow pumping startup or
Stop；
The macromolecule gas-water separation component, it is arranged in aqueous accumulator tank close to the water and hydrogen efferent duct of hydrogen delivery outlet
End, it is by water and Hydrogen Separation and aqueous is back in aqueous accumulator tank, and hydrogen is to be drawn by hydrogen delivery outlet for making
With；
According to above-mentioned field plate, pure water is by pure water storage tank through water filling pumping pressurization, ion exchange resin filter element filtering and stream
Control valve control imports hydrogen-oxygen water electrolyzer, water electrolysis is exported the water of reduction and oxygen to pure water storage tank after acting on and collects
Aqueous simultaneously discharges oxygen, separately exports the water of reduction and hydrogen to aqueous accumulator tank and by macromolecule via water and hydrogen efferent duct
Water and Hydrogen Separation are made aqueous be back in aqueous accumulator tank by gas-water separation component, and hydrogen is drawn by hydrogen delivery outlet and supplied
Use.
In an embodiment of the present utility model, input pipe is provided with a drainpipe therebetween, for giving off pure water storage during maintenance
Aqueous in groove and in input pipe.
In an embodiment of the present utility model, the macromolecule gas-water separation component, for by the hydrogen and aqueous vapor of output
Separation, make moisture-free in the hydrogen that offer uses, above-mentioned macromolecule gas-water separation component, which is provided with Hydrogen Vapor Pressure detection
End, the Hydrogen Vapor Pressure test side and control board are electrically connected with, and Hydrogen Vapor Pressure test side is detecting the pressure of hydrogen delivery outlet
Power state.
In an embodiment of the present utility model, the macromolecule gas-water separation component, it is provided with not in upper and lower in tubular membrane group
Become rusty steel mesh, intermediate arrangement stainless shot, separately sets gas permeable polymer film in the superiors, passes through the hydrogen aqueous vapor containing hydrogen and moisture
Macromolecule gas-water separation component and hydrogen and aqueous are separated, and the aqueous of separation is back to by macromolecule gas-water separation component
Aqueous accumulator tank.
It is well known that the electrical conductivity of general running water is about 150 μ s/cm μ, pure water is about 50 μ s/cm, ultra-pure water is about 3 μ
Below s/cm, pure water is used in the utility model field plate, and predominantly pure water compared with free from admixture and passes through ion exchange resin filter core
Filtering, and the ultra-pure water of intimate standard can be obtained to carry out water electrolysis method generation hydrogen, its can extension device service life.
The utility model is given up with physics high-low water level difference principle water intake mode in traditional water electrolysis method, but with water injecting pump
Pu pressurization is intake in a manner of reducing the vapour lock in pipeline, and it is closed again coordinates flow control valve running, therefore its yield can reach production
The hydrogen gone out is 300-600ml/min, and the hydrogen purity of output is about 99.9995% hydrogen of pure hydrogen.
It is using control board and touch control display interface control power supply and pure water input supply hydrogen-oxygen water electrolyzer, through electricity
Caused water and oxygen and water are exported with hydrogen after solution, wherein the water exported is with hydrogen and will by macromolecule gas-water separation component
Water and Hydrogen Separation, wherein by hydrogen output for use, and aqueous is back to aqueous accumulator tank and leads to pure water storage tank makes for circulation
With also same but oxygen is expelled directly out oxygen water.
According to combinations as those above mode, obtain according to this and reduce pipeline and produce aqueous vapor resistance when preventing that aqueous from flowing by pumping pressurization
Simplify structure and the good field plate of efficiency.
Brief description of the drawings
Fig. 1 is the utility model field plate structural representation.
Fig. 2 is the macromolecule gas-water separation component diagrammatic cross-section of the utility model field plate.
Description of reference numerals：1- power supply units；2- control boards；3- touch control display interfaces；4- hydrogen-oxygen water electrolyzers；
41- water and oxygen output tube；42- water and hydrogen efferent duct；5- pure water storage tanks；51- pure water hand-holes；52- oxygen taps；
53- pure water liquid level sensors；54- input pipes；55- water filling pumpings；56- drainpipes；6- ion exchange resin filter cores；7- flows control
Valve；8- aqueous accumulator tanks；81- hydrogen delivery outlets；82- recycle-water liquid level sensors；83- return ducts；84- backflow pumpings；9- is high
Molecule gas-water separation component；91- Hydrogen Vapor Pressures test side；92- stainless (steel) wires；93- stainless shots；94- gas permeable polymer films.
Embodiment
Shown in Figure 1, the utility model field plate is mainly comprising a power supply unit (1), a control board
(2), a touch control display interface (3), a hydrogen-oxygen water electrolyzer (4), a pure water storage tank (5), an ion exchange resin filter core (6), one stream
The components such as control valve (7), an aqueous accumulator tank (8) and a macromolecule gas-water separation component (9).
The power supply unit (1), for the power input of the field plate, it is connected to control board (2).
The control board (2), which is provided with control circuit and with touch control display interface (3) and hydrogen-oxygen water electrolyzer (4)
It is electrically connected with.
The touch control display interface (3), it is operator and the interface of the control circuit communication of control board (2), including refers to
Order input, hydrogen generation state and hydrogen output flow information are shown.
The hydrogen-oxygen water electrolyzer (4), its anode tap are provided with a water and oxygen output tube (41) and are connected to pure water storage tank
(5) and cathode terminal is provided with a water and hydrogen efferent duct (42) and is connected to aqueous accumulator tank (8), water and hydrogen efferent duct (42)
By aqueous accumulator tank (8) and it is connected to the hydrogen delivery outlet (81) set above aqueous accumulator tank (8).
The pure water storage tank (5), its upper end are provided with pure water hand-hole (51) and oxygen tap (52), storage tank and are provided with pure water
Liquid level sensor (53).
Above-mentioned pure water hand-hole (51), injection end is supplied for pure water source, pure water storage tank (5) the bottom side is provided with an input pipe
(54), input pipe (54) other end is connected to hydrogen-oxygen water electrolyzer (4), and the input pipe (54) is in pure water storage tank (5) and hydrogen-oxygen water
Water filling pumping (55) is provided between electrolyzer (4), is made in the pressurized injection hydrogen-oxygen water electrolyzer (4) of the pure water in pure water storage tank (5)
Carry out water electrolysis effect.
Above-mentioned pure water liquid level sensor (53) and water filling pumping (55) are electrically connected to control board (2), make pure water liquid
Level sensor (53) measures the water level information in pure water storage tank (5) and is transferred to the electric control circuit of control board (2), make into
The row control input of pure water and starting or stoping for water filling pumping (55).
Above-mentioned input pipe (54), therebetween provided with a drainpipe (56), for giving off in pure water storage tank (5) and inputting during maintenance
Manage the aqueous in (54).
Ion exchange resin filter core (6), on above-mentioned input pipe (54), there is provided filtering input hydrogen-oxygen water electrolyzer (4)
Pure water, to promote the purity of pure water and improve electrolysis effectiveness.
The flow control valve (7), it is between the input pipe (54) of hydrogen-oxygen water electrolyzer (4) front end, flow control valve (7)
And control board (2) is electrically connected to, the pure water input quantity of control input pipe (54), makes to reach optimal water electrolysis effect according to this
Energy.
The aqueous accumulator tank (8), its upper end are provided with hydrogen delivery outlet (81), are provided with recycle-water liquid level sensor in accumulator tank
(82)。
Above-mentioned aqueous accumulator tank (8), the aqueous that hydrogen and water are produced for the reduction of hydrogen-oxygen water electrolyzer (4) electrolyzing pure water reclaim
The aqueous accumulator tank utilized, pure water storage tank (5) the bottom side are provided with a return duct (83), and return duct (83) other end is connected to pure
Water storage tank (5), the return duct (83) are provided with backflow pumping (84) between aqueous accumulator tank (8) and pure water storage tank (5), return aqueous
Receive that the withdrawal water in groove (8) is pressurized to be back to pure water storage tank (5).
Recycle-water liquid level sensor (82) and backflow pumping (84) in above-mentioned aqueous accumulator tank (8) are electrically connected to control
Circuit board (2), recycle-water liquid level sensor (82) is measured the water level information of aqueous accumulator tank (8) and be transferred to control board
(2) control circuit, make to be controlled starting or stoping for backflow pumping (84).
The macromolecule gas-water separation component (9), it is to be arranged in aqueous accumulator tank (8) close to hydrogen delivery outlet (81)
Water and hydrogen efferent duct (42) end, it is by water and Hydrogen Separation and aqueous is back in aqueous accumulator tank (8), and hydrogen
It is to be drawn by hydrogen delivery outlet (81) for using.
The macromolecule gas-water separation component (9), its main purpose system separate the hydrogen of output and aqueous vapor, make offer use
Hydrogen in moisture-free.
Above-mentioned macromolecule gas-water separation component (9), which is provided with Hydrogen Vapor Pressure test side (91), the Hydrogen Vapor Pressure test side
(91) it is electrically connected with control board (2), Hydrogen Vapor Pressure test side (91) are detecting the pressure shape of hydrogen delivery outlet (81)
State.
Join shown in Fig. 2, the macromolecule gas-water separation component (9), lie in and upper and lower in tubular membrane group be provided with stainless (steel) wire
(92), intermediate arrangement stainless shot (93), gas permeable polymer film (94) separately is set in the superiors, makes the hydrogen water containing hydrogen and moisture
Gas separates through macromolecule gas-water separation component (9) and by hydrogen and aqueous, and makes the aqueous of separation by macromolecule gas-water separation
Component (9) is back to aqueous accumulator tank (8).
According to upper structure composition, pure water is filtered by pure water storage tank (5) through water filling pumping (55) pressurization, ion exchange resin filter core (6)
And flow control valve (7) control imports hydrogen-oxygen water electrolyzer (4), water electrolysis is set to export the water of reduction and oxygen to pure after acting on
Water storage tank (5) collects aqueous and discharges oxygen, separately exports the water of reduction and hydrogen to water via water and hydrogen efferent duct (42)
Liquid accumulator tank (8) and by macromolecule gas-water separation component (9) by water and Hydrogen Separation, and aqueous is back to aqueous accumulator tank
(8) in, and hydrogen is drawn for using by hydrogen delivery outlet (81).
It is described above to be merely exemplary for the utility model, and nonrestrictive, those of ordinary skill in the art
Understand, in the case where not departing from the spirit and scope that claims appended below is limited, many modifications can be made, change,
Or it is equivalent, but fall within the scope of protection of the utility model.
Claims (4)
1. a kind of field plate, it is characterised in that show comprising a power supply unit (1), a control board (2), a touch-control
Show interface (3), a hydrogen-oxygen water electrolyzer (4), a pure water storage tank (5), an ion exchange resin filter core (6), flow control valve (7),
One aqueous accumulator tank (8) and a macromolecule gas-water separation component (9)；
The power supply unit (1), for the power input of the field plate, it is connected to control board (2)；
The control board (2), electrically connect provided with control circuit and with touch control display interface (3) and hydrogen-oxygen water electrolyzer (4)
Connect；
The touch control display interface (3), it is operator and the interface of the control circuit communication of control board (2)；
The hydrogen-oxygen water electrolyzer (4), its cathode terminal be provided with a water and oxygen output tube (41) and be connected to pure water storage tank (5) and
Anode tap is provided with a water and hydrogen efferent duct (42) and is connected to aqueous accumulator tank (8), and water passes through water with hydrogen efferent duct (42)
Liquid accumulator tank (8) is simultaneously connected to the hydrogen delivery outlet (81) set above aqueous accumulator tank (8)；
The pure water storage tank (5), its upper end are provided with pure water hand-hole (51) and oxygen tap (52), storage tank and are provided with pure water liquid level
Sensor (53), above-mentioned pure water hand-hole (51), injection end is supplied for pure water source, it is defeated that pure water storage tank (5) the bottom side is provided with one
Enter pipe (54), input pipe (54) other end is connected to hydrogen-oxygen water electrolyzer (4), and the input pipe (54) is in pure water storage tank (5) and hydrogen
Water filling pumping (55) is provided between oxygen water electrolyzer (4), makes the pressurized injection hydrogen-oxygen water electrolyzer of the pure water in pure water storage tank (5)
(4) water electrolysis effect is carried out in, above-mentioned pure water liquid level sensor (53) and water filling pumping (55) are electrically connected to control board
(2), for controlling the input of pure water and starting or stoping for water filling pumping (55)；
The ion exchange resin filter core (6), on above-mentioned input pipe (54), there is provided the pure water of filtering input hydrogen-oxygen water electrolyzer (4),
To promote the purity of pure water and improve electrolysis effectiveness；
The flow control valve (7), between the input pipe (54) of hydrogen-oxygen water electrolyzer (4) front end, flow control valve (7) is electrical for it
Control board (2) is connected to, according to this pure water input quantity of control input pipe (54), makes to reach optimal water electrolysis efficiency；
The aqueous accumulator tank (8), its upper end are provided with hydrogen delivery outlet (81), are provided with recycle-water liquid level sensor in accumulator tank
(82), above-mentioned aqueous accumulator tank (8), the aqueous recovery profit of hydrogen and water is produced for the reduction of hydrogen-oxygen water electrolyzer (4) electrolyzing pure water
Aqueous accumulator tank, pure water storage tank (5) the bottom side are provided with a return duct (83), and return duct (83) other end is connected to pure water storage
Groove (5), the return duct (83) are provided with backflow pumping (84) between aqueous accumulator tank (8) and pure water storage tank (5), make aqueous accumulator tank
(8) withdrawal water in is pressurized to be back to pure water storage tank (5), the recycle-water liquid level sensor in above-mentioned aqueous accumulator tank (8)
(82) and backflow pumping (55) is electrically connected to control board (2), for controlling starting or stoping for backflow pumping (84)；
The macromolecule gas-water separation component (9), it is arranged in aqueous accumulator tank (8) close to the water and hydrogen of hydrogen delivery outlet (81)
Efferent duct (42) end, it is by water and Hydrogen Separation and aqueous is back in aqueous accumulator tank (8), and hydrogen is defeated by hydrogen
(81) extraction portal for using；
According to above-mentioned field plate, pure water is by pure water storage tank (5) through water filling pumping (55) pressurization, ion exchange resin filter core (6) mistake
Filter and flow control valve (7) control import hydrogen-oxygen water electrolyzer (4), make water electrolysis act on after by the water of reduction and oxygen export to
Pure water storage tank (5) collects aqueous and discharges oxygen, separately exports the water of reduction and hydrogen extremely via water and hydrogen efferent duct (42)
Aqueous accumulator tank (8) and by macromolecule gas-water separation component (9) by water and Hydrogen Separation, aqueous is back to aqueous accumulator tank
(8) in, and hydrogen is drawn for using by hydrogen delivery outlet (81).
2. field plate according to claim 1, it is characterised in that input pipe (54) is provided with a drainpipe therebetween
(56), for giving off the aqueous in pure water storage tank (5) and in input pipe (54) during maintenance.
3. field plate according to claim 1, it is characterised in that the macromolecule gas-water separation component (9), for inciting somebody to action
Hydrogen and the aqueous vapor separation of output, make moisture-free in the hydrogen that offer uses, above-mentioned macromolecule gas-water separation component (9), its
It is provided with Hydrogen Vapor Pressure test side (91), the Hydrogen Vapor Pressure test side (91) is electrically connected with control board (2), Hydrogen Vapor Pressure
Test side (91) is detecting the pressure state of hydrogen delivery outlet (81).
4. field plate according to claim 3, it is characterised in that the macromolecule gas-water separation component (9), in tubular
It is upper and lower in film group to be provided with stainless (steel) wire (92), intermediate arrangement stainless shot (93), separately set gas permeable polymer film in the superiors
(94) the hydrogen aqueous vapor containing hydrogen and moisture is separated through macromolecule gas-water separation component (9) and by hydrogen and aqueous, and make
The aqueous of separation is back to aqueous accumulator tank (8) by macromolecule gas-water separation component (9).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720348293.1U CN206970719U (en) | 2017-04-05 | 2017-04-05 | Field plate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201720348293.1U CN206970719U (en) | 2017-04-05 | 2017-04-05 | Field plate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206970719U true CN206970719U (en) | 2018-02-06 |
Family
ID=61414486
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201720348293.1U Active CN206970719U (en) | 2017-04-05 | 2017-04-05 | Field plate |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206970719U (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108315755A (en) * | 2018-02-26 | 2018-07-24 | 深圳市量子氢生物技术有限公司 | A kind of hydrogen-rich cup |
| CN108468062A (en) * | 2018-06-04 | 2018-08-31 | 泉州泉氢生物科技有限公司 | Micro-integrated hydrogen gas generation |
| CN109957812A (en) * | 2019-05-14 | 2019-07-02 | 深圳市贺正科技有限公司 | A kind of electrochemistry producing equipment of ultra-pure hydrogen and ultrapure oxygen |
| CN110055547A (en) * | 2019-03-15 | 2019-07-26 | 北京建元天地环保科技有限公司 | A kind of hydrogen production plant by water electrolysis |
| WO2024022926A3 (en) * | 2022-07-28 | 2024-03-21 | John Cockerill Hydrogen Belgium | Waste water recovery system |
-
2017
- 2017-04-05 CN CN201720348293.1U patent/CN206970719U/en active Active
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108315755A (en) * | 2018-02-26 | 2018-07-24 | 深圳市量子氢生物技术有限公司 | A kind of hydrogen-rich cup |
| CN108468062A (en) * | 2018-06-04 | 2018-08-31 | 泉州泉氢生物科技有限公司 | Micro-integrated hydrogen gas generation |
| CN108468062B (en) * | 2018-06-04 | 2024-05-14 | 泉州泉氢生物科技有限公司 | Miniature integrated hydrogen generator |
| CN110055547A (en) * | 2019-03-15 | 2019-07-26 | 北京建元天地环保科技有限公司 | A kind of hydrogen production plant by water electrolysis |
| CN109957812A (en) * | 2019-05-14 | 2019-07-02 | 深圳市贺正科技有限公司 | A kind of electrochemistry producing equipment of ultra-pure hydrogen and ultrapure oxygen |
| WO2024022926A3 (en) * | 2022-07-28 | 2024-03-21 | John Cockerill Hydrogen Belgium | Waste water recovery system |
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