CN206385260U - A kind of modularization hydrogen formation apparatus - Google Patents
A kind of modularization hydrogen formation apparatus Download PDFInfo
- Publication number
- CN206385260U CN206385260U CN201621421826.6U CN201621421826U CN206385260U CN 206385260 U CN206385260 U CN 206385260U CN 201621421826 U CN201621421826 U CN 201621421826U CN 206385260 U CN206385260 U CN 206385260U
- Authority
- CN
- China
- Prior art keywords
- gas
- water tank
- electrolytic cell
- control module
- energy supply
- 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
- 239000001257 hydrogen Substances 0.000 title claims abstract description 48
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 48
- 230000015572 biosynthetic process Effects 0.000 title claims abstract description 13
- 125000004435 hydrogen atom Chemical class [H]* 0.000 title claims 6
- 239000007788 liquid Substances 0.000 claims abstract description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 239000007789 gas Substances 0.000 claims abstract description 37
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 7
- 238000002845 discoloration Methods 0.000 claims description 6
- 238000009413 insulation Methods 0.000 claims description 4
- 230000005611 electricity Effects 0.000 claims description 3
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 abstract description 29
- 150000002431 hydrogen Chemical class 0.000 abstract description 13
- 238000004519 manufacturing process Methods 0.000 abstract description 9
- 229910000831 Steel Inorganic materials 0.000 abstract description 3
- 230000007547 defect Effects 0.000 abstract description 3
- 239000010959 steel Substances 0.000 abstract description 3
- 238000002360 preparation method Methods 0.000 abstract description 2
- 239000012153 distilled water Substances 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 4
- 239000002828 fuel tank Substances 0.000 description 4
- 239000001301 oxygen Substances 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000003054 catalyst Substances 0.000 description 3
- 238000001035 drying Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 238000012423 maintenance Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000011232 storage material Substances 0.000 description 1
Classifications
-
- 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
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model belongs to technical field of hydrogen preparation, specifically related to a kind of modularization hydrogen formation apparatus, including gas circuit, shell, energy supply control module and water tank, water tank includes electrolytic cell, electrolytic cell includes electrolytic cell anode and cathode of electrolytic tank, the top of water tank is provided with liquid feeding steam vent, gas-liquid separator is connected with by gas circuit above the left side of water tank, the left end of gas-liquid separator is connected with pressure maintaining valve in turn by gas circuit, change colour silica dehydrator pipe and four-way valve, one end of four-way valve is connected by gas circuit with shell, one end is connected with external pressure gauge, one end is connected with pressure controller, energy supply control module bottom is provided with control board.The purpose is to：The problem of solving existing hydrogen producer design defect and have that gas storage cylinder gas-storing capacity is limited, its interior gas can only change steel cylinder after being finished, and inconvenient to carry, and security is poor, space-consuming is big, weight is big, inconvenience is installed in production, and need manual discharge opeing.
Description
Technical field
The utility model belongs to technical field of hydrogen preparation, and in particular to a kind of modularization hydrogen formation apparatus.
Background technology
Hydrogen producer, general built-in hydrogen generator, hydrogen generator is a kind of self-adjustable hydrogen for hydrogen fuel cell
Gas generator.The equipment includes consisting of：The fuel tank of one definable inner space with nominal volume, the fuel tank
Equipped with the hydrogen discharge mouthful communicated with inner space；Containing hydrogen storage material and the catalyst in fuel tank is stored in, wherein
Catalyst is filled in catalytic reactor, the reactor equipped with part is closed, can be used to block catalyst and fuel liquid it
Between contact, and the opening portion being in contact with fuel liquid, therefore can actively be adjusted according to the lifting of pressure in fuel tank
It is whole whether to generate hydrogen or stop hydrogen generation.
And existing hydrogen producer has following defect and deficiency：
Gas storage cylinder gas-storing capacity is limited, and its interior gas can only change steel cylinder after being finished, and inconvenient to carry, and security is poor.
Equipment, which occurs, for hydrogen needs to configure multiple parts such as electrolytic cell, electrode, water tank simultaneously, and space-consuming is big, weight
Greatly, inconvenience is installed in production.
Steam is had while gas processed or liquid enters gas circuit, the burden of drying tube is added, drier is accelerated more
Frequency is changed, and needs manual discharge opeing.
Utility model content
The utility model purpose is：A kind of modularization hydrogen formation apparatus is aimed to provide, for solving existing hydrogen producer
Design defect has that gas storage cylinder gas-storing capacity is limited, and its interior gas can only change steel cylinder after being finished, and inconvenient to carry, security
Difference, space-consuming is big, weight is big, inconvenience is installed in production, and the problem of need manual discharge opeing.
To realize above-mentioned technical purpose, the technical solution adopted in the utility model is as follows：
A kind of modularization hydrogen formation apparatus, including gas circuit, shell, energy supply control module and water tank, the water tank
Including electrolytic cell, the electrolytic cell includes electrolytic cell anode and cathode of electrolytic tank, the positive pole of the energy supply control module and electrolysis
Pond anode electrical connection, the negative pole of the energy supply control module is electrically connected with cathode of electrolytic tank, and the top of the water tank, which is provided with, to be added
It is connected with below gas-liquid separator, the gas-liquid separator and is passed through by gas circuit above liquid steam vent, the left side of the water tank
Connected below the left side of gas circuit and water tank, the left end of the gas-liquid separator is connected with pressure maintaining valve, discoloration in turn by gas circuit
Silica dehydrator pipe and four-way valve, the four-way valve are electrically connected with energy supply control module, one end of the four-way valve by gas circuit with
Shell is connected, and one end is connected with external pressure gauge, and one end is connected with pressure controller；The energy supply control module bottom is provided with control
Circuit board processed, the pressure controller is electrically connected with control board.
Using the utility model of above-mentioned technical proposal, water tank is added into a certain amount of distilled water, then power supply mould
Block is powered to water tank, hydrogen is made by being electrolysed distilled water electrolytic cell anode, oxygen is made in cathode of electrolytic tank, what anode was produced
Oxygen is discharged by the liquid feeding steam vent above water tank, and the hydrogen that negative electrode is produced is divided by the gas circuit positioned at negative pole into gas-liquid
From device, the liquid that hydrogen is brought into enters gas-liquid separator, is back to water tank by the pipeline below gas-liquid separator, hydrogen is then
Pressure maintaining valve is flowed to, then flows into discoloration silica dehydrator pipe processing is dried, the hydrogen of obtained drying is flowed through by tracheae pipeline
Four-way valve, finally flows out from the pipeline of shell.The circuit theory is wherein controlled to be：By pressure controller, preset pressure value, when up to
During to higher limit, pressure controller sends signal to energy supply control module, and energy supply control module powers off positive and negative electrode, stops production
Raw hydrogen, when pressure is less than lower limit, pressure controller sends signal to energy supply control module, and energy supply control module is to positive and negative
Pole is powered, and regenerates hydrogen, and realization is automatically controlled, simple to operate.The device electrolytic cell and retaining are tank integrated, simplify electricity
The equipment for solving water hydrogen manufacturing, reduces the volume and cost of hydrogen generator, increases the area of electrode, improve gas production rate,
With time space it is small, lightweight, produce it is easy for installation.Using the start and stop of pressure controller control device, automatically control, operation letter
Single, gas-liquid separator returns liquid automatically, without manual discharge opeing, and hydrogen is directly entered next stage processing unit.
Further limit, sealed insulation pad is provided between the electrolytic cell anode and cathode of electrolytic tank, such structure is set
Meter, can guarantee that electrolytic cell anode and cathode of electrolytic tank are definitely separated, has both saved cost and space, the face of electrode is increased again
Product, gas production rate is higher.
Further limit, liquid level gauge is connected with the right side of the water tank, the liquid level gauge is located on shell, such knot
Structure is designed, and can be convenient for people to, by observing liquid level gauge, add distilled water into water tank in time.
Further limit, the left side of the energy supply control module, which is provided with the left of radiator, the shell, is provided with fan, this
The structure design of sample, reduces the temperature in casing, extends the service life of equipment, reduces plant maintenance number of times.
Further limit, the control board is also associated with charactron, and the charactron is arranged on shell, such
Structure design, can facilitate operating personnel intuitively to observe gas flow.
Brief description of the drawings
The nonlimiting examples that the utility model can be provided by accompanying drawing are further illustrated；
Fig. 1 is a kind of structural representation of modularization hydrogen formation apparatus embodiment of the utility model；
Main element symbol description is as follows：
Liquid level gauge 1, cathode of electrolytic tank 2, sealed insulation pad 3, electrolytic cell anode 4, gas-liquid separator 5, pressure maintaining valve 6, discoloration
Silica dehydrator pipe 7, pressure gauge 8, four-way valve 9, pressure controller 10, energy supply control module 11, radiator 12, fan 13, number
Pipe 14, control board 15, shell 16 and liquid feeding steam vent 17.
Embodiment
In order that the utility model may be better understood in those skilled in the art, it is right with reference to the accompanying drawings and examples
Technical solutions of the utility model are further illustrated.
As shown in figure 1, a kind of modularization hydrogen formation apparatus of the present utility model, including gas circuit, shell 16, power supply
Module 11 and water tank, water tank include electrolytic cell, and electrolytic cell includes electrolytic cell anode 4 and cathode of electrolytic tank 2, power supply mould
The positive pole of block 11 is electrically connected with electrolytic cell anode 4, and the negative pole of energy supply control module 11 is electrically connected with cathode of electrolytic tank 2, water tank
Top be provided with below liquid feeding steam vent 17, the left side of water tank gas-liquid separator 5, gas-liquid separator 5 be connected with by gas circuit
Connected below the left side that lower section passes through gas circuit and water tank, the left end of gas-liquid separator 5 is connected with pressure maintaining valve in turn by gas circuit
6th, discoloration silica dehydrator pipe 7 and four-way valve 9, four-way valve 9 are electrically connected with energy supply control module 11, and one end of four-way valve 9 passes through gas
Road is connected with shell 16, and one end is connected with external pressure gauge 8, and one end is connected with pressure controller 10；The bottom of energy supply control module 11
Portion is provided with control board 15, and pressure controller 10 is electrically connected with control board 15.
Preferably, sealed insulation pad 3, such structure design, energy are provided between electrolytic cell anode 4 and cathode of electrolytic tank 2
Ensure that electrolytic cell anode 4 and cathode of electrolytic tank 2 are definitely separated, both saved cost and space, the area of electrode is increased again, produce
Gas velocity rate is higher.In fact, can also be considered to obstruct the knot of electrolytic cell anode 4 and cathode of electrolytic tank 2 according to actual concrete condition
Configuration formula.
Preferably, liquid level gauge 1 is connected with the right side of water tank, liquid level gauge 1 is located on shell 16, such structure design,
It can be convenient for people to, by observing liquid level gauge 1, add distilled water into water tank in time.In fact, being also designed to other structures
Form observes the number of distilled water in water tank, such as hole is opened up on the side wall of water tank, is provided with hole interior sealing
Transparent panel etc..
Preferably, the left side of energy supply control module 11 is provided with radiator 12, and the left side of shell 16 is provided with fan 13, such
Structure design, reduces the temperature in casing 16, extends the service life of equipment, reduces plant maintenance number of times.In fact,
The structure radiated to energy supply control module 11 can be considered also according to actual concrete condition.
Preferably, control board 15 is also associated with charactron 14, and charactron 14 is arranged on shell, and such structure is set
Meter, can facilitate operating personnel intuitively to observe gas flow.In fact, can also consider observation according to actual concrete condition
The structure of gas flow.
In the present embodiment, water tank is added into a certain amount of distilled water, then energy supply control module 11 is powered to water tank,
Hydrogen is made by being electrolysed distilled water electrolytic cell anode 4, oxygen is made in cathode of electrolytic tank 2, and the oxygen that anode is produced passes through retaining
Liquid feeding steam vent 17 above tank is discharged, and the hydrogen that negative electrode is produced enters gas-liquid separator 5, hydrogen by the gas circuit positioned at negative pole
The liquid brought into enters gas-liquid separator 5, is back to water tank by the pipeline of the lower section of gas-liquid separator 5, hydrogen is then flowed to surely
Pressure valve 6, then flow into discoloration silica dehydrator pipe 7 processing is dried, the hydrogen of obtained drying flows through four-way by tracheae pipeline
Valve 9, finally flows out from the pipeline of shell 16.The circuit theory is wherein controlled to be：By pressure controller 10, preset pressure value, when
When reaching higher limit, pressure controller 10 sends signal to energy supply control module 11, and energy supply control module 11 breaks positive and negative electrode
Electricity, stops producing hydrogen, and when pressure is less than lower limit, pressure controller 10 sends signal, power supply to energy supply control module 11
Control module 11 is powered to both positive and negative polarity, regenerates hydrogen, and realization is automatically controlled, simple to operate.The device electrolytic cell and retaining
Equipment that is tank integrated, simplifying water electrolysis hydrogen production, reduces the volume and cost of hydrogen generator, increases the face of electrode
Product, improve gas production rate, with time space it is small, lightweight, produce it is easy for installation.Use opening for the control device of pressure controller 10
Stop, automatically control, simple to operate, gas-liquid separator returns liquid automatically, without manual discharge opeing, hydrogen is directly entered next stage processing dress
Put.
The merely exemplary explanation principle of the present utility model of above-described embodiment and its effect are new not for this practicality is limited
Type.Any person skilled in the art can all be carried out without prejudice under spirit and scope of the present utility model to above-described embodiment
Modifications and changes.Therefore, all those of ordinary skill in the art are without departing from the spirit disclosed in the utility model
With all equivalent modifications completed under technological thought or change, it should be covered by claim of the present utility model.
Claims (5)
1. a kind of modularization hydrogen formation apparatus, including gas circuit, shell (16), energy supply control module (11) and water tank, it is special
Levy and be：The water tank includes electrolytic cell, and the electrolytic cell includes electrolytic cell anode (4) and cathode of electrolytic tank (2), the electricity
The positive pole of source control module (11) is electrically connected with electrolytic cell anode (4), the negative pole and electrolytic cell of the energy supply control module (11)
Negative electrode (2) is electrically connected, and the top of the water tank, which is provided with above liquid feeding steam vent (17), the left side of the water tank, passes through gas circuit
It is connected with by being connected below the left side of gas circuit and water tank below gas-liquid separator (5), the gas-liquid separator (5), it is described
The left end of gas-liquid separator (5) is connected with pressure maintaining valve (6), discoloration silica dehydrator pipe (7) and four-way valve (9) in turn by gas circuit,
The four-way valve (9) is electrically connected with energy supply control module (11), and one end of the four-way valve (9) is connected by gas circuit and shell (16)
Logical, one end is connected with external pressure gauge (8), and one end is connected with pressure controller (10)；Energy supply control module (11) bottom
Provided with control board (15), the pressure controller (10) electrically connects with control board (15).
2. a kind of modularization hydrogen formation apparatus according to claim 1, it is characterised in that：The electrolytic cell anode (4)
Sealed insulation pad (3) is provided between cathode of electrolytic tank (2).
3. a kind of modularization hydrogen formation apparatus according to claim 2, it is characterised in that：Connect on the right side of the water tank
Liquid level gauge (1) is connected to, the liquid level gauge (1) is located on shell (16).
4. a kind of modularization hydrogen formation apparatus according to claim 3, it is characterised in that：The energy supply control module
(11) left side is provided with radiator (12), and shell (16) left side is provided with fan (13).
5. a kind of modularization hydrogen formation apparatus according to claim 4, it is characterised in that：The control board (15)
Charactron (14) is also associated with, the charactron (14) is arranged on shell (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621421826.6U CN206385260U (en) | 2016-12-23 | 2016-12-23 | A kind of modularization hydrogen formation apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621421826.6U CN206385260U (en) | 2016-12-23 | 2016-12-23 | A kind of modularization hydrogen formation apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206385260U true CN206385260U (en) | 2017-08-08 |
Family
ID=59490297
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621421826.6U Expired - Fee Related CN206385260U (en) | 2016-12-23 | 2016-12-23 | A kind of modularization hydrogen formation apparatus |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206385260U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107672439A (en) * | 2017-08-18 | 2018-02-09 | 广东卓梅尼技术股份有限公司 | A kind of hydrogen hybrid powder integrated control system |
-
2016
- 2016-12-23 CN CN201621421826.6U patent/CN206385260U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107672439A (en) * | 2017-08-18 | 2018-02-09 | 广东卓梅尼技术股份有限公司 | A kind of hydrogen hybrid powder integrated control system |
| CN107672439B (en) * | 2017-08-18 | 2020-10-27 | 广东卓梅尼技术股份有限公司 | Hydrogen hybrid power integrated control system |
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| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| DD01 | Delivery of document by public notice |
Addressee: HUIZHONGXIANG ENVIRONMENTAL PROTECTION TECHNOLOGY HEBEI Co.,Ltd. Person in charge of patents Document name: Notice of Termination of Patent Rights |
|
| DD01 | Delivery of document by public notice | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20170808 |
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| CF01 | Termination of patent right due to non-payment of annual fee |