CN204589318U - The general hydrogen production device of brine electrolysis hyperoxia - Google Patents
The general hydrogen production device of brine electrolysis hyperoxia Download PDFInfo
- Publication number
- CN204589318U CN204589318U CN201520179307.2U CN201520179307U CN204589318U CN 204589318 U CN204589318 U CN 204589318U CN 201520179307 U CN201520179307 U CN 201520179307U CN 204589318 U CN204589318 U CN 204589318U
- Authority
- CN
- China
- Prior art keywords
- hydrogen
- separator
- electrolyzer
- oxygen
- pure water
- 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
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
Abstract
The utility model relates to water electrolysis hydrogen production breathing equipment technical field, be specifically related to the general hydrogen production device of a kind of brine electrolysis hyperoxia, comprise electrolyzer, electrolyzer is connected with hydrogen separator, oxygen separator, hydrogen separator connects purifier, electrolyzer connects pure water tank, pure water tank is provided with inlet mouth and air outlet, hydrogen separator is connected with water cooler and steam separator in turn by hydrogen pipeline, air outlet on pure water tank is communicated with the hydrogen pipeline between hydrogen separator and water cooler, oxygen separator connects purifier by oxygen pipeline, purifier comprises the dehydrogenation agent adsorption tanks connected successively, water cooler, steam separator and molecular sieve adsorption tank, this device is by electrolysis, be separated, purifying obtains high purity oxygen gas and common hydrogen, industrial application can be directly used in, simplify industrial flow and industrial cost.
Description
Technical field
The utility model relates to water electrolysis hydrogen production breathing equipment technical field, is specifically related to the general hydrogen production device of a kind of brine electrolysis hyperoxia.
Background technology
Device for preparing hydrogen is applied in multiple field, and the gas that it produces comprises hydrogen and oxygen two kinds, is widely used in the industries such as oil, chemical industry, metallurgy, medicine, when industrial application, has certain requirement to the purity of gas.Existing small electrolytic water device for producing hydrogen, the oxygen produced can not utilize very well, generally all can directly emit, such waste is very little, and for large-scale device for preparing hydrogen, its amount of oxygen produced is comparatively large, can not ignore, directly emit if select, larger waste can be caused; Usually containing gaseous impuritieies such as nitrogen in brine electrolysis, can mix with the oxyhydrogen produced during electrolysis, have impact on the oxyhydrogen purity of generation.
Utility model content
According to above deficiency of the prior art, the technical problems to be solved in the utility model is: provide a kind of brine electrolysis hyperoxia general hydrogen production device, obtain high purity oxygen gas and common hydrogen by electrolysis, separation, purifying, can industrial application be directly used in, simplify industrial flow and industrial cost.
The general hydrogen production device of brine electrolysis hyperoxia described in the utility model, comprise electrolyzer, electrolyzer is connected with hydrogen separator, oxygen separator, hydrogen separator connects purifier, electrolyzer connects pure water tank, pure water tank is provided with inlet mouth and air outlet, and hydrogen separator is connected with water cooler and steam separator in turn by hydrogen pipeline, and the air outlet on pure water tank is communicated with the hydrogen pipeline between hydrogen separator and water cooler; Oxygen separator connects purifier by oxygen pipeline, and purifier comprises the dehydrogenation agent adsorption tanks, water cooler, steam separator and the molecular sieve adsorption tank that connect successively.
Electrolytic tank electrolysis water produces hydrogen and oxygen, these two kinds of gases are separated by respective separator, the oxygen separated is undertaken dewatering by purifier, dehydrogenation purification process, final formation hyperoxia, the hydrogen separated carries out processed by water cooler and steam separator, pure water in electrolyzer is from pure water tank, pure water tank there is inlet, outlet, hydrogen blowback pure water can be led to, physical property is utilized to be taken away by the gaseous impurities in pure water, then pass into hydrogen pipeline, the hydrogen produced with brine electrolysis mixes, the general hydrogen of final formation.
Be provided with molding machine between described dehydrogenation agent adsorption tanks and water cooler, by the oxygen compression separated, improve purification process working efficiency.
Water cooler on described hydrogen pipeline is connected with hydrogen compressor, hydrogen-pressure can be reduced to required specified pressure and stores.
Be provided with water pump between described pure water tank and electrolyzer, the pure water in pure water tank can be delivered in electrolyzer by water pump fast.
The beneficial effect that the utility model is compared with prior art had is:
The general hydrogen production device of brine electrolysis hyperoxia is rational in infrastructure, high purity oxygen gas and common hydrogen is obtained by electrolysis, separation, purifying, in pure water tank, water conservancy hydrogen to be electrolysed is carried out blowback, reduce the gaseous impurities in brine electrolysis, further increase the purity that brine electrolysis generates gas, and the hydrogen that the hydrogen of blowback and electrolysis produce mixes, carry out reclaiming again, the compressible storage of oxyhydrogen that this device generates, is directly used in industrial application, simplifies industrial flow and industrial cost.
Accompanying drawing explanation
Fig. 1 is the utility model structural representation.
In figure: 1, inlet mouth; 2, pure water tank; 3, water pump; 4, electrolyzer; 5, molecular sieve adsorption tank; 6, steam separator; 7, water cooler; 8, molding machine; 9, dehydrogenation agent adsorption tanks; 10, oxygen pipeline; 11, oxygen separator; 12, hydrogen separator; 13, hydrogen pipeline; 14, hydrogen compressor; 15, air outlet.
Embodiment
Below in conjunction with accompanying drawing, embodiment of the present utility model is described further:
As shown in Figure 1, the general hydrogen production device of brine electrolysis hyperoxia, comprise electrolyzer 4, electrolyzer 4 is connected with hydrogen separator 12, oxygen separator 11, hydrogen separator 12 connects purifier, and electrolyzer 4 connects pure water tank 2, and pure water tank 2 is provided with inlet mouth 1 and air outlet 15, hydrogen separator 12 is connected with water cooler 7 and steam separator 6 in turn by hydrogen pipeline 13, and the air outlet 15 on pure water tank 2 is communicated with the hydrogen pipeline 13 between hydrogen separator 12 and water cooler 7; Oxygen separator 11 connects purifier by oxygen pipeline 10, and purifier comprises the dehydrogenation agent adsorption tanks 9, water cooler 7, steam separator 6 and the molecular sieve adsorption tank 5 that connect successively.
Molding machine 8 is provided with between dehydrogenation agent adsorption tanks 9 and water cooler 7.
Water cooler 7 on hydrogen pipeline 13 is connected with hydrogen compressor 14.
Water pump 3 is provided with between pure water tank 2 and electrolyzer 4.
During the work of this device, hydrogen is passed into from the inlet mouth 1 pure water tank 2, utilize hydrogen blowback pure water, the physical property of gas is utilized to be taken away by the gaseous impuritieies such as the nitrogen in pure water, then gas passes into hydrogen pipeline 13 from air outlet 15, the pure water of blowback enters electrolyzer 4 by water pump 3, electrolyzer 4 brine electrolysis produces hydrogen and oxygen, oxygen is separated by oxygen separator 11, enter dehydrogenation agent adsorption tanks 9 dehydrogenation of purifier, then enter molding machine 8 to compress, enter purifier again and carry out deep dehydration purification, final formation hyperoxia, hydrogen is separated by hydrogen separator 12, the hydrogen passed into air outlet 15 in hydrogen pipeline 13 mixes, then specified pressure is compressed to hydrogen compressor 14 as required, processed is carried out again by water cooler 7 and steam separator 6, the general hydrogen of final formation.
Claims (4)
1. the general hydrogen production device of brine electrolysis hyperoxia, comprise electrolyzer (4), electrolyzer (4) is connected with hydrogen separator (12), oxygen separator (11), hydrogen separator (12) connects purifier, it is characterized in that: electrolyzer (4) connects pure water tank (2), pure water tank (2) is provided with inlet mouth (1) and air outlet (15), hydrogen separator (12) is connected with water cooler (7) and steam separator (6) in turn by hydrogen pipeline (13), air outlet (15) on pure water tank (2) is communicated with the hydrogen pipeline (13) between hydrogen separator (12) and water cooler (7), oxygen separator (11) connects purifier by oxygen pipeline (10), and purifier comprises the dehydrogenation agent adsorption tanks (9), water cooler (7), steam separator (6) and the molecular sieve adsorption tank (5) that connect successively.
2. the general hydrogen production device of brine electrolysis hyperoxia according to claim 1, is characterized in that: be provided with molding machine (8) between described dehydrogenation agent adsorption tanks (9) and water cooler (7).
3. the general hydrogen production device of brine electrolysis hyperoxia according to claim 1 and 2, is characterized in that: the water cooler (7) on described hydrogen pipeline (13) is connected with hydrogen compressor (14).
4. the general hydrogen production device of brine electrolysis hyperoxia according to claim 3, is characterized in that: be provided with water pump (3) between described pure water tank (2) and electrolyzer (4).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520179307.2U CN204589318U (en) | 2015-03-27 | 2015-03-27 | The general hydrogen production device of brine electrolysis hyperoxia |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520179307.2U CN204589318U (en) | 2015-03-27 | 2015-03-27 | The general hydrogen production device of brine electrolysis hyperoxia |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204589318U true CN204589318U (en) | 2015-08-26 |
Family
ID=53925490
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520179307.2U Expired - Fee Related CN204589318U (en) | 2015-03-27 | 2015-03-27 | The general hydrogen production device of brine electrolysis hyperoxia |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204589318U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108330502A (en) * | 2018-02-28 | 2018-07-27 | 佛山市熙华科技有限公司 | A kind of floatation type hydrogen-rich oxygen machine |
-
2015
- 2015-03-27 CN CN201520179307.2U patent/CN204589318U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108330502A (en) * | 2018-02-28 | 2018-07-27 | 佛山市熙华科技有限公司 | A kind of floatation type hydrogen-rich oxygen machine |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207745676U (en) | The recovery and processing system of technique of trichlorosilane synthetic tail gas | |
| CN210340328U (en) | Integrated continuous oxygen and nitrogen making device | |
| CN204589320U (en) | The general oxygen device of brine electrolysis height hydrogen | |
| CN203923390U (en) | The device of a kind of brine electrolysis high purity oxygen processed | |
| CN102173382B (en) | Byproduct hydrogen purification recovery system and method in chlorine industry | |
| CN204589318U (en) | The general hydrogen production device of brine electrolysis hyperoxia | |
| CN1328159C (en) | Equipment and technological process for preparing nitrogen trifluoride by using ammonia and hydrogen fluoride as raw material | |
| CN104709877B (en) | One kind reclaims nitrogen and hydrogen device and method in synthesis ammonia relief gas | |
| CN104030485A (en) | Device for carrying out impurity removal treatment on crude brine for electrolysis and treatment method using same | |
| CN202030521U (en) | Purifying and recovering system for byproduct hydrogen in chlor-alkali industry | |
| CN205347592U (en) | Processing apparatus is decomposed with light salt aquatic chlorate to electrolysis | |
| TWI427035B (en) | A device for producing ammonia | |
| CN204589317U (en) | Water electrolysis prepares pure hydrogen system | |
| CN204589321U (en) | Water electrolysis is utilized to prepare pure hydrogen and oxygen reclamation system | |
| CN206692741U (en) | The ultrapure hydrogen production device of electrolysis water system | |
| CN203488980U (en) | Device for filling high-purity acetylene and industrial acetylene simultaneously | |
| CN201942759U (en) | All-in-one machine for gas and liquid separation and oxygen purification of water electrolysis hydrogen manufacturing | |
| CN104498983A (en) | Method for preparation of high purity oxygen by water electrolysis | |
| CN109847555B (en) | Device and method for recovering multiple gases in catalytic dry gas based on hydrate method | |
| CN215208468U (en) | Hydrogen purification system in chlor-alkali tail gas | |
| TWI434822B (en) | A manufacture method of methanol and its device thereof | |
| CN204973822U (en) | A many functional response cauldron for epoxy plasticizer production | |
| CN111285329A (en) | Method for obtaining hydrogen energy from chlor-alkali industry | |
| CN203959955U (en) | Crude brine removal of impurities treatment unit for electrolysis | |
| CN203612949U (en) | Hydrogen purification section system for sodium chlorate production |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20150826 Termination date: 20160327 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |