CN203960347U - With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function - Google Patents
With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function Download PDFInfo
- Publication number
- CN203960347U CN203960347U CN201420283404.1U CN201420283404U CN203960347U CN 203960347 U CN203960347 U CN 203960347U CN 201420283404 U CN201420283404 U CN 201420283404U CN 203960347 U CN203960347 U CN 203960347U
- Authority
- CN
- China
- Prior art keywords
- bubble
- hydrogen
- decollator
- oxygen
- gas
- 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 - Lifetime
Links
- 239000007789 gas Substances 0.000 title claims abstract description 47
- 239000000203 mixture Substances 0.000 title claims abstract description 40
- 239000001257 hydrogen Substances 0.000 title claims abstract description 29
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 29
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 title claims abstract description 26
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 title claims abstract description 19
- 229910001882 dioxygen Inorganic materials 0.000 title claims abstract description 19
- 230000009711 regulatory function Effects 0.000 title claims abstract description 10
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 13
- 239000008151 electrolyte solution Substances 0.000 claims abstract description 13
- 150000002431 hydrogen Chemical class 0.000 claims abstract description 5
- 230000001105 regulatory effect Effects 0.000 claims description 10
- 239000007788 liquid Substances 0.000 claims description 9
- 230000008676 import Effects 0.000 claims description 3
- 239000002699 waste material Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 abstract description 14
- 239000001301 oxygen Substances 0.000 abstract description 14
- 229910052760 oxygen Inorganic materials 0.000 abstract description 14
- 230000000630 rising effect Effects 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000009434 installation Methods 0.000 description 2
- 239000008186 active pharmaceutical agent Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003245 working effect Effects 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 relates to a kind of hydrogen and oxygen gas mixture generating unit with gas ratio regulatory function, this hydrogen and oxygen gas mixture generating unit comprises: electrolyzer body, in described electrolyzer body, be provided with and in one, hold portion, in this, hold bubble decollator is installed in portion, described bubble decollator upper surface offers some lower concentric annular grooves, and described bubble decollator is also communicated with an air line, this air line passes the bottom of holding portion and electrolyzer body in described downwards, is connected with the air feeder that is arranged on electrolyzer body exterior.The utility model is blown into bubble by air feeder, bubble decollator on the intrinsic battery lead plate of electrolyzer, the oxygen producing on can accelerating electrode plate or hydrogen gas bubbles depart from battery lead plate, can also alleviate the rising of electrolytic solution and battery lead plate temperature, in air, oxygen mixes with the gas that electrolysis produces simultaneously, can regulate the oxygen-hydrogen ratio in mixed gas, increase the content of oxygen, thereby reduce the oxynitride that burning produces, and stop hydrogen split pole phenomenon.
Description
Technical field:
The utility model relates to hydrogen and oxygen gas mixture generation equipment technical field, refers in particular to the board-like hydrogen and oxygen gas mixture generating unit of a kind of vertical ring electrode with gas ratio regulatory function.
Background technology:
Oxygen/hydrogen gas mixture generating unit is by ionization water of decomposition, thereby obtain the device of oxygen and hydrogen, in the electrolyzer that positive and negative electrode is installed, put into the water with a small amount of electrolysed substance, pass to volts DS, produce oxygen respectively and hydrogen at the two poles of the earth, and discharge after mixing in electrolyzer.
In airtight electrolyzer, the mixture ratio of oxygen and hydrogen is 1:2, and in long-play process, this mixture ratio remains constant, and therefore, the combustioncharacteristics of this mixed gas is very single, can not be applicable to need the situation of other combustioncharacteristicss; And the gas mixture of this ratio is known from experience because burning generates oxynitride (NOx) in a large number, this can cause environmental pollution; In addition, along with the carrying out of electrolysis, the temperature of electrolytic solution can rise, and can hinder flowing of electric current, thereby the phenomenon such as loss of voltage, hydrogen split pole often occurs, and sometimes needing shutdown to restart after temperature lowers can.
In addition, existing water electrolyzer is generally horizontal setting, battery lead plate in it is parallel equidistant, positive and negative staggered arrangement, battery lead plate mostly is zigzag wave shape wave, positive and negative electrode is arranged in electrolyzer by an electrode fixed strip suspending respectively, and this frame mode is installed less stable, easily loosening, deflection of battery lead plate in the process that works long hours, can cause that partial electrolysis is unbalanced, the problems such as efficiency is low of giving vent to anger, also the battery lead plate life-span be caused to disadvantageous effect.
Utility model content:
Problem to be solved in the utility model is exactly to solve the problems referred to above that scheme is brought in the past, provides a kind of vertical ring electrode with gas ratio regulatory function board-like hydrogen and oxygen gas mixture generating unit.
The technical scheme that the utility model is realized its object employing is: the board-like hydrogen and oxygen gas mixture generating unit of a kind of vertical ring electrode with gas ratio regulatory function, and this hydrogen and oxygen gas mixture generating unit comprises:
Be vertical tubular, hold the electrolyzer body of electrolytic solution, electrolyzer body upper end open, periphery is provided with notch flange and is sealed and installed with electro bath-lid; On electro bath-lid, offer electrolytic solution import and mixed gas outlet; The bottom of electrolyzer body offers waste liquid relief outlet and circulation of elecrolyte outlet, and electrolyzer body middle part is provided with circulation of elecrolyte entrance, between circulation of elecrolyte outlet and circulation of elecrolyte entrance, is communicated with recycle pump;
In described electrolyzer body, be provided with and in one, hold portion, in this, hold bubble decollator is installed in portion, described bubble decollator upper surface offers some lower concentric annular grooves, and described bubble decollator is also communicated with an air line, this air line passes the bottom of holding portion and electrolyzer body in described downwards, is connected with the air feeder that is arranged on electrolyzer body exterior;
Be provided with the electrode upper mounted plate relative with bubble decollator in the below of described electro bath-lid, the lower surface of described electrode upper mounted plate also offers the upper concentric annular groove relative with lower concentric annular groove; Between electrode upper mounted plate and bubble decollator, some battery lead plates concentric, positive and negative staggered arrangement that are are installed; And the center of described electrode upper mounted plate, bubble decollator is also provided with the electrode axis being electrically connected with battery lead plate, described electrode axis passes described electro bath-lid outside hermetically.
Described air feeder comprises air supply device, bubble jet pressure regulating part, the mixed gas composition ratio configuration part being connected with bubble jet pressure regulating part being connected with air supply device and the microprocessor that connects and control described bubble jet pressure regulating part and mixed gas composition ratio configuration part; At described mixed gas outlet place, gas flow/composition inductor block is also installed, and described gas flow/composition inductor block is also connected with described microprocessor.
Described electrolyzer body is assembled by upper groove body and lower groove, described in the portion of holding be arranged between upper groove body and lower groove, in hold the passage that is equipped with the circulation of electrolysis liquid on portion and bubble decollator.
The bottom of described battery lead plate offers the opening of electrolysis liquid circulation, and the top of battery lead plate offers the gas stream through hole for hydrogen and oxygen gas mixture circulation.
Technique effect of the present utility model is mainly reflected in: the utility model is blown into bubble by air feeder, bubble decollator on the intrinsic battery lead plate of electrolyzer, the oxygen producing on can accelerating electrode plate or hydrogen gas bubbles depart from battery lead plate, promote the carrying out of electrolysis, air bubble can also be alleviated the rising of electrolytic solution and battery lead plate temperature, in air, oxygen mixes with the gas that electrolysis produces simultaneously, can regulate the oxygen-hydrogen ratio in mixed gas, increase the content of oxygen, thereby reduce the oxynitride that burning produces, and stop hydrogen split pole phenomenon.
Brief description of the drawings:
Fig. 1 is the sectional view of the utility model knallgas generating unit;
Fig. 2, Fig. 3 are the schematic diagram of battery lead plate in the utility model;
Fig. 4 is the principle schematic that the utility model mixed gas ratio regulates.
Embodiment:
Below in conjunction with specific embodiments and the drawings, the utility model is further illustrated.
As shown in Figure 1, the board-like hydrogen and oxygen gas mixture generating unit of vertical ring electrode described in the utility model, this hydrogen and oxygen gas mixture generating unit comprises:
Be vertical tubular, hold the electrolyzer body 1 of electrolytic solution, electrolyzer body 1 upper end open, periphery is provided with notch flange 101 and is sealed and installed with electro bath-lid 2; On electro bath-lid 2, offer electrolytic solution import 201 and mixed gas outlet 202; The bottom of electrolyzer body 1 offers waste liquid relief outlet 102 and circulation of elecrolyte outlet 103, electrolyzer body 1 middle part is provided with circulation of elecrolyte entrance 104, between circulation of elecrolyte outlet 103 and circulation of elecrolyte entrance 104, be communicated with recycle pump (in figure for illustrating), recycle pump is arranged on electrolyzer body 1 outside, connects circulation of elecrolyte outlet 103 and circulation of elecrolyte entrance 104 by water pipe.
In described electrolyzer body 1, be provided with in one and hold portion 3, hold in portion 3 bubble decollator 4 is installed in this, described bubble decollator 4 upper surfaces offer some lower concentric annular grooves 41;
In described electrolyzer body 1, be provided with and in one, hold portion 3, in this, hold bubble decollator 4 is installed in portion 3, described bubble decollator 4 upper surfaces offer some lower concentric annular grooves 41, and described bubble decollator 4 is also communicated with an air line 42, this air line 42 passes the bottom of holding portion 3 and electrolyzer body 1 in described downwards, is connected with the air feeder 43 that is arranged on electrolyzer body 1 outside;
Be provided with the electrode upper mounted plate 5 relative with bubble decollator 4 in the below of described electro bath-lid 2, the lower surface of described electrode upper mounted plate 5 also offers the upper concentric annular groove 51 relative with lower concentric annular groove 41; Between electrode upper mounted plate 5 and bubble decollator 4, some battery lead plates 6 concentric, positive and negative staggered arrangement that are are installed; And the center of described electrode upper mounted plate 5, bubble decollator 4 is also provided with the electrode axis 61 being electrically connected with battery lead plate 6, described electrode axis 61 passes described electro bath-lid 2 outsides hermetically by electrode axis permanent sleeve 62.
In the utility model, bubble decollator 4, except coordinating and provide bubble with air feeder, also plays with electrode upper mounted plate and matches, the effect of fixed plate electrode 6.
Shown in Fig. 4, described air feeder 43 comprises air supply device 431, bubble jet pressure regulating part 432, the mixed gas composition ratio configuration part 433 being connected with bubble jet pressure regulating part 432 being connected with air supply device 431 and the microprocessor 434 that connects and control described bubble jet pressure regulating part 432 and mixed gas composition ratio configuration part 433; At described mixed gas outlet, 202 places are also provided with gas flow/composition inductor block 435, and described gas flow/composition inductor block 435 is also connected with described microprocessor 434.Gas flow/composition inductor block 435 is by the flow at the mixed gas outlet sensing 202 places, component ratio converts data signal to and feeds back to microprocessor 434, microprocessor 434 can be according to the data of induction and the Data Comparison set of mixed gas composition ratio configuration part 433, further adjust the set(ting)value of mixed gas composition ratio, and produce command signal control bubble jet pressure regulating part 432, and then the supply gas pressure of adjusting air supply device 431, make amount and the speed of air feed, pressure change, reach the effect that changes and regulate oxygen hydrogen gas mixture composition ratio.
Described electrolyzer body 1 is assembled by upper groove body 11 and lower groove 12, hold portion 3 in described to be arranged between upper groove body 11 and lower groove 12, in hold the passage (not shown) that is equipped with the circulation of electrolysis liquid on portion 3 and bubble decollator 4.
As shown in Figure 2 and Figure 3, the bottom of described battery lead plate 6 offers the opening 601 of electrolysis liquid circulation, and the top of battery lead plate 6 offers the gas stream through hole 602 for hydrogen and oxygen gas mixture circulation.Described battery lead plate 6 be shaped as annular or just polygon annular, between adjacent battery lead plate, be radially spaced set.
Technique effect of the present utility model is mainly reflected in: on the battery lead plate 6 in electrolyzer body 1, be blown into bubble by air feeder 43, bubble decollator 4, the oxygen producing on can accelerating electrode plate or hydrogen gas bubbles depart from battery lead plate, promote the carrying out of electrolysis, air bubble can also be alleviated the rising of electrolytic solution and battery lead plate temperature, in air, oxygen mixes with the gas that electrolysis produces simultaneously, can regulate the oxygen-hydrogen ratio in mixed gas, increase the content of oxygen, thereby reduce the oxynitride that burning produces, and stop hydrogen split pole phenomenon.
The utility model arranges the battery lead plate 6 of the vertical installation of concentric ring form, be fixed installation by electrode upper and lower fixing plate, guarantee that battery lead plate 6 there will not be loosening, deflection, thereby ensure electrolytic efficiency uniformity, guarantee gas efficiency and extend battery lead plate work-ing life.In addition, the utility model also arranges circulation of elecrolyte pipeline, and circulation of elecrolyte is flowed, and guarantees that electrolytic solution is evenly distributed, and mobile electrolytic solution is also conducive to make bubble more easily to depart from battery lead plate, is beneficial to the cooling of electrolytic solution and improves gas efficiency.
Interest field of the present utility model is not limited only to the above embodiments and distortion example, but can in another attached patent claimed range, be presented as diversity examples of implementation too.Do not depart from the utility model main idea requiring in patent claimed range, in the technical field described in this utility model, various scope that every people with common knowledge can be out of shape, is all considered as within the scope of claimed range record of the present utility model.
Claims (4)
1. the hydrogen and oxygen gas mixture generating unit with gas ratio regulatory function, is characterized in that: this hydrogen and oxygen gas mixture generating unit comprises:
Be vertical tubular, hold the electrolyzer body of electrolytic solution, electrolyzer body upper end open, periphery is provided with notch flange and is sealed and installed with electro bath-lid; On electro bath-lid, offer electrolytic solution import and mixed gas outlet; The bottom of electrolyzer body offers waste liquid relief outlet and circulation of elecrolyte outlet, and electrolyzer body middle part is provided with circulation of elecrolyte entrance, between circulation of elecrolyte outlet and circulation of elecrolyte entrance, is communicated with recycle pump;
In described electrolyzer body, be provided with and in one, hold portion, in this, hold bubble decollator is installed in portion, described bubble decollator upper surface offers some lower concentric annular grooves, and described bubble decollator is also communicated with an air line, this air line passes the bottom of holding portion and electrolyzer body in described downwards, is connected with the air feeder that is arranged on electrolyzer body exterior;
Be provided with the electrode upper mounted plate relative with bubble decollator in the below of described electro bath-lid, the lower surface of described electrode upper mounted plate also offers the upper concentric annular groove relative with described lower concentric annular groove; Between electrode upper mounted plate and bubble decollator, some battery lead plates concentric, positive and negative staggered arrangement that are are installed; And the center of described electrode upper mounted plate, bubble decollator is also provided with the electrode axis being electrically connected with battery lead plate, described electrode axis passes described electro bath-lid outside hermetically.
2. the hydrogen and oxygen gas mixture generating unit with gas ratio regulatory function according to claim 1, is characterized in that: described air feeder comprises air supply device, bubble jet pressure regulating part, the mixed gas composition ratio configuration part being connected with bubble jet pressure regulating part being connected with air supply device and the microprocessor that connects and control described bubble jet pressure regulating part and mixed gas composition ratio configuration part; At described mixed gas outlet place, gas flow/composition inductor block is also installed, and described gas flow/composition inductor block is also connected with described microprocessor.
3. the hydrogen and oxygen gas mixture generating unit with gas ratio regulatory function according to claim 1, it is characterized in that: described electrolyzer body is assembled by upper groove body and lower groove, in described, the portion of holding is arranged between upper groove body and lower groove, in hold the passage that is equipped with the circulation of electrolysis liquid on portion and bubble decollator.
4. the hydrogen and oxygen gas mixture generating unit with gas ratio regulatory function according to claim 1, it is characterized in that: the bottom of described battery lead plate offers the opening of electrolysis liquid circulation, the top of battery lead plate offers the gas stream through hole for hydrogen and oxygen gas mixture circulation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420283404.1U CN203960347U (en) | 2014-05-29 | 2014-05-29 | With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420283404.1U CN203960347U (en) | 2014-05-29 | 2014-05-29 | With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203960347U true CN203960347U (en) | 2014-11-26 |
Family
ID=51920955
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420283404.1U Expired - Lifetime CN203960347U (en) | 2014-05-29 | 2014-05-29 | With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203960347U (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108385123A (en) * | 2018-01-30 | 2018-08-10 | 广西奔科衷新能源有限公司 | It is a kind of quickly for the device of engine hydrogen and oxygen mixture |
| CN108425127A (en) * | 2018-01-30 | 2018-08-21 | 广西奔科衷新能源有限公司 | A kind of device quickly preparing hydrogen and oxygen mixture |
| CN110023543A (en) * | 2017-02-23 | 2019-07-16 | 川崎重工业株式会社 | The operation method of water electrolysis system and water electrolysis system |
| CN113073338A (en) * | 2021-03-19 | 2021-07-06 | 深圳市创辉氢科技发展有限公司 | Electrolytic cell |
-
2014
- 2014-05-29 CN CN201420283404.1U patent/CN203960347U/en not_active Expired - Lifetime
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110023543A (en) * | 2017-02-23 | 2019-07-16 | 川崎重工业株式会社 | The operation method of water electrolysis system and water electrolysis system |
| CN110023543B (en) * | 2017-02-23 | 2021-05-25 | 川崎重工业株式会社 | Water electrolysis system and method for operating water electrolysis system |
| CN108385123A (en) * | 2018-01-30 | 2018-08-10 | 广西奔科衷新能源有限公司 | It is a kind of quickly for the device of engine hydrogen and oxygen mixture |
| CN108425127A (en) * | 2018-01-30 | 2018-08-21 | 广西奔科衷新能源有限公司 | A kind of device quickly preparing hydrogen and oxygen mixture |
| CN113073338A (en) * | 2021-03-19 | 2021-07-06 | 深圳市创辉氢科技发展有限公司 | Electrolytic cell |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN203960347U (en) | With the hydrogen and oxygen gas mixture generating unit of gas ratio regulatory function | |
| CN106365260A (en) | Hydrogen-rich water electrolytic bath | |
| CN203960348U (en) | The board-like hydrogen and oxygen gas mixture generating unit of vertical ring electrode | |
| CN109487292A (en) | A kind of method and apparatus generating hydrogen and oxygen using membrane electrode | |
| CN205115612U (en) | Novel super -pure hydrogen generator | |
| HK1138642A1 (en) | Internal flow control in electrolytic cells | |
| CN203834032U (en) | Burner system for generating hydrogen-oxygen mixed gas by electrolyzing water | |
| CN115011983B (en) | Alkaline water electrolysis bath device with multiple current input binding posts | |
| CN203653710U (en) | Bipolar membrane pole distance electrolytic cell with circulating pipe | |
| RU2007123894A (en) | PLANT FOR PRODUCING MINERAL MELT BY PLASMA HEATING | |
| CN203271957U (en) | Car electrolytic cell generating oxyhydrogen and car combustion-supporting oxyhydrogen generation system | |
| CN104372369A (en) | Water electrolysis bath unit capable of adjusting oxygen / hydrogen mixture ratio | |
| CN201933160U (en) | Natural circulation ion-exchange membrane electrolytic cell | |
| CN104047765A (en) | Oxyhydrogen oil-saving device | |
| CN206051636U (en) | A kind of device for removing phosphorous by electrolysis | |
| CN211546680U (en) | Hydrogen generator for producing hydrogen by hydrogen-oxygen separation | |
| CN205634887U (en) | Structure ozone generator concatenates | |
| CN204644478U (en) | A kind of hydrogen generating device | |
| KR20100028965A (en) | Nascent oxygen hydrogen water of electrolysis | |
| CN100574854C (en) | Method for purifying ultra-vast water and purifier | |
| CN103436913B (en) | The device of a kind of electro deposited nickel or electrodeposited cobalt | |
| CN203862411U (en) | Electrolytic flotation column | |
| CN206553246U (en) | A kind of efficient light electrolysis suspension bed apparatus | |
| CN205934038U (en) | Fine preparation adiponitrile electrolysis trough of electrolysis propylene | |
| CN205241848U (en) | Novel stirring of etched foil liquid device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20141126 |