CN203602727U - Hydrogen-oxygen generator - Google Patents
Hydrogen-oxygen generator Download PDFInfo
- Publication number
- CN203602727U CN203602727U CN201320785423.XU CN201320785423U CN203602727U CN 203602727 U CN203602727 U CN 203602727U CN 201320785423 U CN201320785423 U CN 201320785423U CN 203602727 U CN203602727 U CN 203602727U
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- CN
- China
- Prior art keywords
- electrolyzer
- liquid
- hydrogen
- electrolysis
- container
- 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
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Classifications
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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
Abstract
The utility model relates to a hydrogen-oxygen generator for generating hydrogen-oxygen mixed gas by electrolyzing water with direct current. The hydrogen-oxygen generator comprises a body, a main power source on the body, a load line connected with the main power source, an electrolytic cell connected with the load line, a gas outlet formed at the upper end of the electrolytic cell, a liquid return opening formed at the lower end of the electrolytic cell, a liquid storage tank connected with the gas outlet and the liquid return opening, a hydrogen-oxygen conduit connected with the liquid storage tank, and an electrolytic water tank connected with the liquid storage tank, wherein the electrolytic cell is composed of a plurality of electrolytic groups, planar heating panels are arranged between the electrolytic groups, a temperature sensor is arranged between the electrolytic cell and the main power source, a stainless steel radiator is arranged between the gas outlet and the liquid storage tank, a buffer tank and a one-way valve are arranged between the liquid return opening and the liquid storage tank, and a voltage regulator and a flame arrester are arranged between the liquid storage tank and the hydrogen-oxygen conduit. The hydrogen-oxygen generator has the advantages that the temperature of the electrolyte in the electrolytic cell is effectively reduced, the cooling cost of the electrolytic cell is saved, and the electrolytic efficiency is greatly improved, therefore, the hydrogen-oxygen generator can operate more safely and stably.
Description
Technical field
The utility model belongs to a kind of hydrogen and oxygen preparation facilities, particularly a kind of oxyhydrogen generator that utilizes direct current water to be carried out to electrolysis generation hydrogen and oxygen gas mixture.
Background technology
Hydrogen energy source is more and more subject to people's favor as the novel environment friendly energy, oxyhydrogen generator can produce hydrogen and oxygen by water electrolysis simultaneously, be mainly used in the cutting of various non-ferrous metals, metal fusion welding, ampoule wire-drawing, carbon steel cutting, pharmaceutical factory's aqueous injection drawing seal and other various flame machining etc., domestic existing oxyhydrogen generator is mature on the whole aspect electrolytic circuit, but because electrolyzer heats up too fast, easily cause the problem of ageing of rubber and gas leakage, although by encloses container being carried out to electrolyzer encapsulation and strengthens electrolyzer liquid storage space playing the effect of heat radiation, but so greatly improve the production cost of electrolyzer, and utilize the installing space that recycle pump heat radiation not only can increasing device, and reduce electrolytic efficiency, increase the probability of device fails.
Utility model content
The utility model object is to overcome the deficiencies in the prior art and a kind of oxyhydrogen generator is provided.
The purpose of this utility model is achieved in that a kind of oxyhydrogen generator, comprise body, be arranged on the primary source on body, the load line being connected with primary source, the electrolyzer being connected with load line, be arranged on the air outlet of electrolyzer upper end, be arranged on the liquid return hole of electrolyzer lower end, the container for storing liquid being connected with air outlet and liquid return hole, with the tank connected oxyhydrogen conduit of liquid storage, by brine electrolysis conduit and the tank connected electrolysis water pot of liquid storage, it is characterized in that: described electrolyzer is made up of multiple electrolysis groups, between electrolysis group, be provided with plane heating panel, between electrolyzer and primary source, be provided with temperature sensor, between air outlet and container for storing liquid, be provided with electrolyzer escape pipe, on electrolyzer escape pipe, be provided with stainless steel heat radiator, between liquid return hole and container for storing liquid, be provided with electrolyzer liquid returning tube, on electrolyzer liquid returning tube, be provided with surge tank and one-way cock, between container for storing liquid and oxyhydrogen airway, be provided with voltate regulator and spark arrester, between container for storing liquid and electrolysis water pot, be provided with water pump and magnetic valve.
In described stainless steel heat radiator, be provided with cooling fan.
Described brine electrolysis tank top is provided with water supplement port, and electrolysis water pot bottom is provided with liquid level switch.
The utlity model has following positively effect: after electrolytic solution is cooling by stainless steel heat radiator, enter container for storing liquid, electrolytic solution is back in electrolyzer by surge tank and electrolyzer liquid returning tube, realize the Physical temperature-lowering of electrolyzer, effectively reduce the temperature of electrolyzer electrolyte inside, make electrolysis temperature be stabilized in 40 ℃-60 ℃, and without active cycle equipment is installed, without encapsulation electrolyzer, eliminated the water spray phenomenon of oxyhydrogen generator simultaneously, under the non-stop-machine state of machine, realize the ability of supplementing at any time brine electrolysis, not only save electrolyzer cooling cost, and greatly increase electrolytic efficiency, oxyhydrogen generator is safely and steadily run more.
Accompanying drawing explanation
Fig. 1 is the structural representation of utility model.
Embodiment
Embodiment 1, as shown in Figure 1, a kind of oxyhydrogen generator, comprise body, be arranged on the primary source 1 on body, the load line 2 being connected with primary source 1, the electrolyzer 3 being connected with load line 2, be arranged on the air outlet 4 of electrolyzer 3 upper ends, be arranged on the liquid return hole 5 of electrolyzer 3 lower ends, the container for storing liquid 6 being connected with air outlet 4 and liquid return hole 5, the oxyhydrogen conduit 7 being connected with container for storing liquid 6, the electrolysis water pot 9 being connected with container for storing liquid 6 by brine electrolysis conduit 8, described electrolyzer 3 is made up of multiple electrolysis groups 10, between electrolysis group 10, be provided with plane heating panel 11, between electrolyzer 3 and primary source 1, be provided with temperature sensor 12, between air outlet 4 and container for storing liquid 6, be provided with electrolyzer escape pipe 16, on electrolyzer escape pipe 16, be provided with stainless steel heat radiator 13, between liquid return hole 5 and container for storing liquid 6, be provided with electrolyzer liquid returning tube 19, on electrolyzer liquid returning tube 19, be provided with surge tank 14 and one-way cock 15, between container for storing liquid 6 and oxyhydrogen airway 7, be provided with voltate regulator 17 and spark arrester 18, between container for storing liquid 6 and electrolysis water pot 9, be provided with water pump 20 and magnetic valve 21, hydrogen and oxygen gas mixture and electrolytic solution arrive container for storing liquid 6 after stainless steel heat radiator 13 is cooling, carry out gas, liquid separates, wherein knallgas is by spark arrester 10, pressure limiting controller 11, being transferred to equipment along knallgas conduit 12 applies outward, electrolytic solution is back in electrolyzer 3 along electrolyzer liquid returning tube 19 by surge tank 14 and one-way cock 15, realize the Physical temperature-lowering of electrolyzer 3, in described stainless steel heat radiator 13, be provided with cooling fan 22, electrolysis water pot 9 tops are provided with water supplement port 23, electrolysis water pot 9 bottoms are provided with liquid level switch 24, along with equipment operation, when equipment Inspection is in container for storing liquid 6 when insufficient electrolyte, water pump 20 and magnetic valve 21 are opened simultaneously, utilize brine electrolysis conduit 8 that the electrolytic solution in electrolysis water pot 9 is pumped in container for storing liquid 6, in supplementing electrolytic solution, also can lower the temperature to electrolytic solution, in the time that electrolysis water pot 9 water levels drop to liquid level switch 24, water pump 20 and magnetic valve 21 are closed, after supplementing brine electrolysis, again water pump 20 and magnetic valve 21 are opened water supplement port 23.
The utility model effectively reduces the temperature of electrolyzer electrolyte inside; make electrolysis temperature be stabilized in 40 ℃-60 ℃; without active cycle equipment is installed; without encapsulation electrolyzer; under the non-stop-machine state of machine, realize the ability of supplementing at any time brine electrolysis, not only save electrolyzer cooling cost; and greatly increased electrolytic efficiency, oxyhydrogen generator is safely and steadily run more.
Claims (3)
1. an oxyhydrogen generator, comprise body, be arranged on the primary source on body, the load line being connected with primary source, the electrolyzer being connected with load line, be arranged on the air outlet of electrolyzer upper end, be arranged on the liquid return hole of electrolyzer lower end, the container for storing liquid being connected with air outlet and liquid return hole, with the tank connected oxyhydrogen conduit of liquid storage, by brine electrolysis conduit and the tank connected electrolysis water pot of liquid storage, it is characterized in that: described electrolyzer is made up of multiple electrolysis groups, between electrolysis group, be provided with plane heating panel, between electrolyzer and primary source, be provided with temperature sensor, between air outlet and container for storing liquid, be provided with electrolyzer escape pipe, on electrolyzer escape pipe, be provided with stainless steel heat radiator, between liquid return hole and container for storing liquid, be provided with electrolyzer liquid returning tube, on electrolyzer liquid returning tube, be provided with surge tank and one-way cock, between container for storing liquid and oxyhydrogen airway, be provided with voltate regulator and spark arrester, between container for storing liquid and electrolysis water pot, be provided with water pump and magnetic valve.
2. oxyhydrogen generator according to claim 1, is characterized in that: in described stainless steel heat radiator, be provided with cooling fan.
3. oxyhydrogen generator according to claim 1, is characterized in that: described brine electrolysis tank top is provided with water supplement port, and electrolysis water pot bottom is provided with liquid level switch.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320785423.XU CN203602727U (en) | 2013-12-04 | 2013-12-04 | Hydrogen-oxygen generator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320785423.XU CN203602727U (en) | 2013-12-04 | 2013-12-04 | Hydrogen-oxygen generator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203602727U true CN203602727U (en) | 2014-05-21 |
Family
ID=50715414
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320785423.XU Expired - Fee Related CN203602727U (en) | 2013-12-04 | 2013-12-04 | Hydrogen-oxygen generator |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203602727U (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106222687A (en) * | 2016-06-29 | 2016-12-14 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
| CN106245052A (en) * | 2016-06-29 | 2016-12-21 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
| CN106854764A (en) * | 2017-03-26 | 2017-06-16 | 安聪聪 | A kind of Novel electrolytic water manufactures oxygen unit |
| CN108950586A (en) * | 2018-08-10 | 2018-12-07 | 绿城农科检测技术有限公司 | A kind of hydrogen generator |
| CN109097789A (en) * | 2018-10-24 | 2018-12-28 | 南京元亨化工科技有限公司 | Convenient for the electrolysis unit of heat dissipation |
| CN111172553A (en) * | 2020-03-16 | 2020-05-19 | 朱树勋 | Multi-core high-efficiency hydrogen and oxygen generator |
| CN113249746A (en) * | 2021-07-01 | 2021-08-13 | 清华大学 | Flow field plate structure of electrolytic cell |
-
2013
- 2013-12-04 CN CN201320785423.XU patent/CN203602727U/en not_active Expired - Fee Related
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106222687A (en) * | 2016-06-29 | 2016-12-14 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment that can quickly add solution |
| CN106245052A (en) * | 2016-06-29 | 2016-12-21 | 唐以松 | A kind of hydro-electrolytic hydroxide mixed gas equipment |
| CN106854764A (en) * | 2017-03-26 | 2017-06-16 | 安聪聪 | A kind of Novel electrolytic water manufactures oxygen unit |
| CN106854764B (en) * | 2017-03-26 | 2018-11-02 | 安聪聪 | A kind of Novel electrolytic water manufacture oxygen unit |
| CN108950586A (en) * | 2018-08-10 | 2018-12-07 | 绿城农科检测技术有限公司 | A kind of hydrogen generator |
| CN108950586B (en) * | 2018-08-10 | 2020-03-31 | 绿城农科检测技术有限公司 | Hydrogen generator |
| CN109097789A (en) * | 2018-10-24 | 2018-12-28 | 南京元亨化工科技有限公司 | Convenient for the electrolysis unit of heat dissipation |
| CN111172553A (en) * | 2020-03-16 | 2020-05-19 | 朱树勋 | Multi-core high-efficiency hydrogen and oxygen generator |
| CN111172553B (en) * | 2020-03-16 | 2023-03-24 | 朱树勋 | Multi-core high-efficiency hydrogen and oxygen generator |
| CN113249746A (en) * | 2021-07-01 | 2021-08-13 | 清华大学 | Flow field plate structure of electrolytic cell |
| CN113249746B (en) * | 2021-07-01 | 2021-09-10 | 清华大学 | Flow field plate structure of electrolytic cell |
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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 | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140521 Termination date: 20211204 |