CN208395285U - Electrolysis unit - Google Patents
Electrolysis unit Download PDFInfo
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- CN208395285U CN208395285U CN201820120226.9U CN201820120226U CN208395285U CN 208395285 U CN208395285 U CN 208395285U CN 201820120226 U CN201820120226 U CN 201820120226U CN 208395285 U CN208395285 U CN 208395285U
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 52
- 239000001257 hydrogen Substances 0.000 claims abstract description 56
- 229910052739 hydrogen Inorganic materials 0.000 claims abstract description 56
- UFHFLCQGNIYNRP-UHFFFAOYSA-N hydrogen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 claims abstract description 54
- 230000000875 corresponding Effects 0.000 claims abstract description 9
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- MYMOFIZGZYHOMD-UHFFFAOYSA-N oxygen Chemical compound data:image/svg+xml;base64,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 data:image/svg+xml;base64,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 O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 2
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- 235000003140 Panax quinquefolius Nutrition 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound 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- 238000003487 electrochemical reaction Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
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- 239000007789 gas Substances 0.000 description 1
- 235000005035 ginseng Nutrition 0.000 description 1
- 235000008434 ginseng Nutrition 0.000 description 1
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- 239000000463 material Substances 0.000 description 1
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Abstract
Electrolysis unit provided by the utility model, comprising: four-way switch, input terminal connects the anode of power supply, control terminal connects controller, there are four ports for output end tool;Electrolytic cell, it is in series by multiple pole plates, an electrolytic chamber is constituted between two neighboring pole plate;And multiple pole plates include: the first end pole plate for connecting power cathode;The setting opposite with first end pole plate and the second end pole plate being connect with an input port;The N number of bipolar plates being spacedly distributed between first end pole plate and second end pole plate;TheA bipolar plates,A bipolar plates,A bipolar plates connect one to one with the other three input port;Controller is connected for controlling the input terminal in four-way switch according to supply voltage with port corresponding in output end.The utility model effectively realizes that hydrogen production plant by water electrolysis to the adaptability of wave motion input power supply, improves efficiency of energy utilization.
Description
Technical field
The utility model relates to electrochemical techniques and replaceable energy technology field more particularly to a kind of electrolysis unit.
Background technique
Hydrogen possesses light weight as energy storage carrier, and energy density is high, when use to environment without any discharge the advantages that, by
To the favor of vast researcher and environmentalist.However, hydrogen is not present in nature, need to utilize external energy
It is prepared.The technology of hydrogen manufacturing at present is mainly fossil fuel hydrogen manufacturing and water electrolysis hydrogen producing two major classes.Also there are other hydrogen production process
Such as thermochemical cycle for hydrogen production and biomass hydrogen preparation.Fossil fuel hydrogen manufacturing is current maximum and most economical hydrogen source, with
Society development and environmental problem receive more and more attention, fossil fuel hydrogen manufacturing use petroleum fuel as former due to it
Material inevitably has certain negative effect during preparing hydrogen to environment, and the prepared hydrogen later period needs cumbersome
Filtering and separation process cause hydrogen purity to be not necessarily able to satisfy the requirement of later period hydrogen storage equipment.In addition, fossil fuel hydrogen manufacturing
Commonly used in large-scale production base, its effect can not be played completely in the micro-capacitance sensor framework of current high-efficiency and economic.
Water electrolysis hydrogen producing obtains the hydrogen of high-purity by electrolysis water, and device structure is mature, relatively easy.It is purified
Hydrogen purity afterwards may be up to 99.9999%, be higher by the not carbon containing member of hydrogen of other hydrogen manufacturing mode an order of magnitude and its preparation
Plain impurity, so become the high-precision application field unique selection of such as production of polysilicon.However the energy transformation ratio of water electrolysis hydrogen producing
It is relatively low to compare fossil fuel hydrogen manufacturing, researchs and analyses and obtains, in the production consumption composition of water electrolysis hydrogen producing, raw material are (predominantly
Electricity charge investment) accounting is up to 81.9%, and cause water electrolysis hydrogen producing in whole hydrogen manufacturing market portion very little.
New energy sustainable development today is vigorously advocated in country, water electrolysis hydrogen producing has welcome new opportunity to develop.It can
The renewable sources of energy such as wind energy, solar energy, tide energy etc. cause big since it produces electricity the unstability and territory restriction of power
Amount renewable energy can not be reasonably utilized, and " abandonment abandons water and abandons light " phenomenon then occur.Water electrolysis hydrogen producing is flexible by it
System scale, mature and stable system performance, and with the good compatible degree of hydrogen fuel cell system, be expected to become mainstream
The technological means of hydrogen manufacturing.On the other hand, hydrogen is as energy carrier, and in the fuel of equal quality, it is close to possess highest energy
Degree.Water electrolysis hydrogen producing will also play the part of important role in terms of energy storage applications and micro-capacitance sensor building in future.
New energy water electrolysis hydrogen producing institute facing challenges mostly come from two aspects at present: water electrolysis hydrogen production is inefficient
And new energy input power is unstable.Therefore, optimization water electrolysis hydrogen producing system is to fluctuation power input (such as renewable energy
Source, such as solar energy, wind energy, tide energy etc.) adaptability, while improving the hydrogen output of unit energy, be current water electrolysis hydrogen producing
The main target of technology.
Therefore, the electrolytic cell for water electrolysis hydrogen producing how is improved to the adaptability of fluctuation power supply, proposes energy conversion effect
Rate is a technical problem to be solved urgently.
Utility model content
The utility model provides a kind of electrolysis unit, for effectively improving the electrolytic cell of water electrolysis hydrogen producing to fluctuation power supply
Adaptability improves energy conversion efficiency, reduces the waste of renewable resource.
To solve the above-mentioned problems, the utility model provides a kind of electrolysis unit, including electrolytic cell, power supply, controller
And four-way switch;Wherein:
The four-way switch, input terminal connects the anode of the power supply, control terminal connects the controller, output end tool
There are first port, second port, third port and the 4th port;
The electrolytic cell, it is in series by multiple pole plates, an electrolytic chamber is constituted between two neighboring pole plate;And it is described more
A pole plate includes: first end pole plate, is set to one end of the electrolytic cell, and connect the cathode of the power supply;Second end pole plate,
The other end that is set to the electrolytic cell opposite with the first end pole plate, and connect with the 4th port;It is N number of bipolar
Plate, N number of bipolar plates are spacedly distributed between the first end pole plate and the second end pole plate;TheA bipolar plates
Connect by contact with the first port,A bipolar plates are connect by contact with the second port, the
A bipolar plates are connect by contact with the third port;Wherein, N is positive integer;
The controller for detecting supply voltage, and is controlled according to the supply voltage defeated in the four-way switch
Enter end to be connected with port corresponding in output end.
It preferably, further include being set to the unidirectional of electrolytic chamber's hydrogen outlet side to hinder back valve in the electrolytic cell.
Electrolysis unit provided by the utility model, the access section of selectivity and the testing result to input power power
Divide electrolytic cell to enter circuit loop, in the case where excessively not increasing production cost, effectively realizes hydrogen production plant by water electrolysis to wave
The adaptability of dynamic input power, improves efficiency of energy utilization, while being renewable energy (such as wind energy, solar energy, tide energy
Deng) collection, storage and transport provide solution.
Detailed description of the invention
Attached drawing 1 is the structural schematic diagram of electrolysis unit in specific embodiment of the present invention;
Attached drawing 2 is the structural schematic diagram that valve is unidirectionally hindered back in specific embodiment of the present invention.
Specific embodiment
It elaborates with reference to the accompanying drawing to the specific embodiment of electrolysis unit provided by the utility model.
Present embodiment provides a kind of electrolysis unit, and attached drawing 1 is electrolysed in specific embodiment of the present invention
The structural schematic diagram of device.As shown in Figure 1, the electrolysis unit that present embodiment provides, including electrolytic cell 9, power supply 6, control
Device 5 and four-way switch 8 processed.Wherein, the power supply 6 is the electric energy generated by renewable energy conversion, such as is produced by wind-power electricity generation
The electric energy etc. that electric energy that raw electric energy, solar energy can be transformed, tide energy are transformed.The electrolytic cell 9 is for being electrolysed
Water is to generate clean energy resource hydrogen, specifically, electrochemical reaction occurs in electrolytic cell 9: by the electric energy of input by water decomposition
At hydrogen and oxygen, wherein hydrogen after removing water purity up to 99.9%.
The four-way switch 8, input terminal connects the anode of the power supply 6, control terminal connects the controller 5, output
End has first port (1), second port (2), third port (3) and the 4th port (4).
Renewable energy electricity generation ability is greatly influenced by objective factors such as weather, for example wind power generation is limited by local wind
Energy intensity and its duration, solar power generation are limited by received sunlight intensity and sunshine-duration.These factors
Result in output voltage fluctuation of the renewable energy as power supply.
In order to adapt to the fluctuation of 6 voltage of the power supply generated by renewable energy, efficiency of energy utilization, this tool are improved
The electrolytic cell 9 in electrolysis unit provided by body embodiment, it is in series by multiple pole plates, between two neighboring pole plate
Constitute an electrolytic chamber, by water electrolysis generate hydrogen process occur in electrolytic chamber, and inside each electrolytic chamber by every
Film is separated into anode and cathode.The multiple pole plate includes N bipolar plates and two unipolar plates, and two unipolar plates include
It is placed in the first end pole plate 1 and second end pole plate 4 of 9 opposite end of electrolytic cell.As shown in Figure 1, the first end pole plate 1,
It is set to one end of the electrolytic cell 9, and connects the cathode of the power supply 6;Second end pole plate 4, with the first end pole plate 1
The opposite other end for being set to the electrolytic cell 9, and connect with the 4th port (4);N number of bipolar plates 2, it is N number of described double
Pole plate 2 is spacedly distributed between the first end pole plate 1 and the second end pole plate 4.I.e. in the electricity of present embodiment
A total of N+2 pole plate in slot 9 is solved, N+1 cell is constituted by this N+2 pole plate altogether, and this N+1 cell is to be serially connected.
For present embodiment in order to adapt to the supply voltage fluctuated, taken mode is the electricity that different number is controlled according to supply voltage
Solve cell access electrolysis circuit.
Specifically, in present embodiment, theA bipolar plates 2 are connected by contact and the first port (1)
Connect,A bipolar plates 2 are connect by contact with the second port (2), theA bipolar plates 2 pass through contact and institute
State third port (3) connection;Wherein, N is positive integer.In this embodiment, four of 8 input terminal of four-way switch
Port connects one to one with four pole plates (i.e. second end pole plate 4 and three bipolar plates).The controller 5, for detecting electricity
Source voltage, and the input terminal in the four-way switch 8 is controlled according to the supply voltage and is connected with port corresponding in output end.
It is connected in this way, controlling the input terminal in the four-way switch 8 by the controller 5 with port corresponding in output end, energy
It is enough to realize by electrolytic chamber's access electrolysis circuit of different number, to complete to make all or part of electricity for different electrical power voltage
Solve the process that cell participates in electrolytic hydrogen production.Preferably, whenWithCalculated result be non-integer when, with right
The value that its calculated result obtains after rounding up is as the bipolar plates connecting with the four-way switch 8.
During carrying out water electrolysis hydrogen production using the electrolysis unit that present embodiment provides, electric current is from the power supply
6 anode outflow after, first pass around the four-way switch 8, from a certain bipolar plates 2 contact or the second end pole plate 4 stream
Enter, then by electrolytic chamber some or all of in electrolytic cell 9, after the power supply 6 is flowed back to after the first end pole plate 1
Cathode.Wherein, show to participate in reacting when the input terminal in the four-way switch 8 is connected with the first port (1) in output end
Electrolytic chamber's minimum number, correspondingly, the 4th port (4) conducting in input terminal and output end in the four-way switch 8
When show that electrolytic chamber whole in the electrolytic cell 9 both participates in reaction (the electrolytic chamber quantity for participating in reaction is maximum).Ginseng
It is fewer with the electrolytic chamber's quantity reacted, then show that power input is smaller compared to the maximum acceptable input power of electrolytic cell.Generally
In the case of, power input power, which is respectively less than electrolytic cell, can receive rated power.
Attached drawing 2 is the structural schematic diagram that valve is unidirectionally hindered back in specific embodiment of the present invention.It is anti-in order to collect electrolysis
The hydrogen that should be generated generally is respectively arranged with hydrogen outlet side and oxygen outlet side in electrolytic chamber.Electricity is participated in order to prevent
The hydrogen generated in the electrolytic chamber of reaction is solved to be back in the electrolytic chamber for having neither part nor lot in cell reaction and occur to be electrolysed back reaction,
It preferably, as shown in Figure 1, 2, further include being set to unidirectionally hindering back for electrolytic chamber's hydrogen outlet side in the electrolytic cell 9
Valve 3.The setting for unidirectionally hindering back valve 3, can further increase the hydrogen output of unit energy, realize the maximization acquisition of hydrogen.
The electrolysis unit that present embodiment provides, selectivity connects and the testing result to input power power
Enter partial electrolyte slot and enter circuit loop, in the case where excessively not increasing production cost, effectively realizes hydrogen production plant by water electrolysis
To the adaptability of wave motion input power supply, efficiency of energy utilization is improved, while being renewable energy (such as wind energy, solar energy, tide
Can be equal) collection, storage and transport solution is provided.
Embodiment 1
Maximum gas production is 1Nm3Electrolytic cell (system is about 5kw) altogether contain 50 electrolytic chamber, pole plate (all pole plates
Count) quantity be 51 pieces.According to the design (referring to Fig.1) of the present embodiment, first end pole plate 1 is connected to renewable energy
The cathode of power supply 6;Second end pole plate 4 is connected to the 4th port (4) of four-way switch 8;51/4th piece of bipolar plates (calculated result
For non-integer, round up to its calculated result, i.e., the 13rd piece of bipolar plates since first end pole plate 1) it is connected to four tunnels
The first port (1) of switch 8;51/2nd piece of bipolar plates (calculated result is non-integer, is rounded up to its calculated result,
The 26th piece of bipolar plates i.e. since first end pole plate 1) it is connected to the second port (2) of four-way switch 8;51*3/4 block bipolar plates
(calculated result is non-integer, is rounded up to its calculated result, i.e., the 39th piece of bipolar plates since first end pole plate 1) connects
It is connected to the third port (3) of four-way switch 8;The input terminal of four-way switch 8 is connected to the anode of renewable energy source current 6;Control
Device 5 is in parallel with renewable energy source current 6, and connect with the control terminal of four-way switch 8, for detecting renewable energy source current 6
Supply voltage.Corresponding electrolysis system capacity can be divided into 5 gears according to present embodiment electrolysis unit current setting: system is closed
(disconnection of four-way switch 8), 1.3kW mode (input terminal in four-way switch is connected with the first port in output end), 2.6kW mould
Formula (input terminal in four-way switch is connected with the second port in output end), 3.9kW mode (input terminal in four-way switch with
In output end third port conducting) and 5kW mode (lead the 4th port in the input terminal and output end in four-way switch
It is logical).
It is illustrated so that the electrolysis unit in the present embodiment is coupled with 5kW photovoltaic array as an example.Before sun rise, photovoltaic
Array does not work, input power zero, and the device of the present embodiment is in system off state at this time;After the sun rises (such as
6am-8am), photovoltaic array is started to work, but illumination incident angle is big at this time, and light ray radiation intensity is not high, and photovoltaic array is defeated
Power is small (such as 1kW) out.The present embodiment electrolysis unit is input to by DC/DC converter built in photovoltaic system and by controller
5 collect, and controller 5 is controlled according to the input power (or voltage) of power supply 6 at this time in the input terminal and output end of four-way switch 8
First port (1) conducting.So far, the present embodiment electrolysis unit works in 1.3kW mode.When the sun continues to rise (8am-
10am), illumination incident angle reduces, light ray radiation enhanced strength, and photovoltaic array output power increases (such as 2.2kW).This electricity
The variation of source power is monitor by the controller 5 in the present embodiment electrolysis unit always, (the ratio when its value reaches preset threshold value
Such as >=1.95kW), control second port (2) conducting in the input terminal and output end of four-way switch 8.As the sun rises
(10am-11am) illumination incidence angle continues to reduce, and light ray radiation intensity continues growing, and the output power of photovoltaic array also continues
Increase (3.5kW), the present embodiment electrolysis unit will run on 3.9kW mode (the i.e. input terminal and output end of four-way switch 8 at this time
In third port (3) conducting).When high noon (11am-1pm) arrives, direct sunlight is in photovoltaic array, and photovoltaic array exports at this time
Its peak value 5kW, corresponding the present embodiment electrolysis unit also run on peak value (5kW) mode (i.e. the input terminal of four-way switch 8 with it is defeated
The 4th port (4) conducting in outlet).Similarly, served as it is afternoon, with the decrease of light ray radiation intensity, photovoltaic array it is defeated
Power is gradually reduced out, and the present embodiment electrolysis unit also regulates and controls its access electricity according to the fluctuation of corresponding renewable energy source current 6
Electrolytic chamber's quantity in road circuit.
It should be pointed out that electrolysis unit is not linear change as described in Example 1, the electricity in present embodiment
Solution device gives corresponding power system capacity (i.e. the port of four-way switch connects) according to the fluctuation of supply voltage to ensure this tool
Body embodiment electrolysis unit is in always on the capacity of optimization, to provide maximum system efficiency.As previously mentioned, this is specific
Embodiment highlights the structure and design of a kind of variable capacity electrolysis unit, wherein four-way switch and 5kW power system capacity
Design is not fixed design, can be adjusted according to actual needs.
The above is only the preferred embodiment of the utility model, it is noted that for the common skill of the art
Art personnel can also make several improvements and modifications without departing from the principle of this utility model, these improvements and modifications
Also it should be regarded as the protection scope of the utility model.
Claims (2)
1. a kind of electrolysis unit, which is characterized in that including electrolytic cell, power supply, controller and four-way switch;Wherein:
The four-way switch, input terminal connects the anode of the power supply, control terminal connects the controller, output end has the
Single port, second port, third port and the 4th port;
The electrolytic cell, it is in series by multiple pole plates, an electrolytic chamber is constituted between two neighboring pole plate;
And the multiple pole plate includes: first end pole plate, is set to one end of the electrolytic cell, and connects the negative of the power supply
Pole;Second end pole plate, the other end that is set to the electrolytic cell opposite with the first end pole plate, and with the 4th port
Connection;N number of bipolar plates, N number of bipolar plates are spacedly distributed between the first end pole plate and the second end pole plate;TheA bipolar plates are connect by contact with the first port, theA bipolar plates are connected by contact and the second port
Connect,A bipolar plates are connect by contact with the third port;Wherein, N is positive integer;
The controller controls the input terminal in the four-way switch for detecting supply voltage, and according to the supply voltage
Port conducting corresponding with output end.
2. electrolysis unit according to claim 1, which is characterized in that further include being set to the electrolysis in the electrolytic cell
Cell hydrogen outlet side unidirectionally hinders back valve.
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Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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CN111826673A (en) * | 2020-08-07 | 2020-10-27 | 阳光电源股份有限公司 | Water electrolysis hydrogen production system based on renewable energy and control method thereof |
CN111945178A (en) * | 2020-08-07 | 2020-11-17 | 涓ュ己 | Off-grid type electrolytic cell structure and electrode control method |
CN111962092A (en) * | 2020-08-17 | 2020-11-20 | 涓ュ己 | Off-grid independent electrolytic cell structure and electrode control method |
CN112647088A (en) * | 2020-08-05 | 2021-04-13 | 严强 | Off-grid electrolysis control structure and mode |
CN113337840A (en) * | 2020-04-13 | 2021-09-03 | 严强 | Off-grid electrolysis control method and structure independent of power grid |
WO2021223570A1 (en) * | 2020-05-02 | 2021-11-11 | Gu Shiping | Energy storage, carbon sequestration and new energy cycle |
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2018
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Publication number | Priority date | Publication date | Assignee | Title |
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CN113337840A (en) * | 2020-04-13 | 2021-09-03 | 严强 | Off-grid electrolysis control method and structure independent of power grid |
WO2021208524A1 (en) * | 2020-04-13 | 2021-10-21 | 严强 | Off-grid electrolysis control method and structure independent of power grid |
WO2021223570A1 (en) * | 2020-05-02 | 2021-11-11 | Gu Shiping | Energy storage, carbon sequestration and new energy cycle |
CN112647088A (en) * | 2020-08-05 | 2021-04-13 | 严强 | Off-grid electrolysis control structure and mode |
CN111945178A (en) * | 2020-08-07 | 2020-11-17 | 涓ュ己 | Off-grid type electrolytic cell structure and electrode control method |
CN111826673A (en) * | 2020-08-07 | 2020-10-27 | 阳光电源股份有限公司 | Water electrolysis hydrogen production system based on renewable energy and control method thereof |
CN111962092A (en) * | 2020-08-17 | 2020-11-20 | 涓ュ己 | Off-grid independent electrolytic cell structure and electrode control method |
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