CN201461148U - Efficient oxy-hydrogen electrolytic bath - Google Patents
Efficient oxy-hydrogen electrolytic bath Download PDFInfo
- Publication number
- CN201461148U CN201461148U CN2009200857809U CN200920085780U CN201461148U CN 201461148 U CN201461148 U CN 201461148U CN 2009200857809 U CN2009200857809 U CN 2009200857809U CN 200920085780 U CN200920085780 U CN 200920085780U CN 201461148 U CN201461148 U CN 201461148U
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- China
- Prior art keywords
- base
- electrolytic solution
- metal electrode
- manifold
- manifolds
- 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
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- 239000001257 hydrogen Substances 0.000 title claims abstract description 21
- 229910052739 hydrogen Inorganic materials 0.000 title claims abstract description 21
- 239000002184 metal Substances 0.000 claims abstract description 41
- 239000007789 gas Substances 0.000 claims abstract description 27
- 239000008151 electrolyte solution Substances 0.000 claims description 45
- 229920006351 engineering plastic Polymers 0.000 claims description 5
- 230000008676 import Effects 0.000 claims description 2
- 239000003792 electrolyte Substances 0.000 abstract description 12
- 238000005868 electrolysis reaction Methods 0.000 abstract description 7
- 230000003071 parasitic effect Effects 0.000 abstract 1
- 239000001301 oxygen Substances 0.000 description 7
- 229910052760 oxygen Inorganic materials 0.000 description 7
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 5
- 150000002431 hydrogen Chemical class 0.000 description 4
- 244000045947 parasite Species 0.000 description 4
- 239000012267 brine Substances 0.000 description 3
- 230000008021 deposition Effects 0.000 description 3
- 239000012535 impurity Substances 0.000 description 3
- 238000002347 injection Methods 0.000 description 3
- 239000007924 injection Substances 0.000 description 3
- 238000009413 insulation Methods 0.000 description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 229910001882 dioxygen Inorganic materials 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000000866 electrolytic etching Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 125000004430 oxygen atom Chemical group O* 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000003466 welding Methods 0.000 description 1
Images
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
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to an efficient oxy-hydrogen electrolytic bath, which comprises a shell, a base, an upper cover, N+1 metal electrode plates, an electrolyte ingress pipe, an electrolyte and gas delivery pipe, N*M upper cover manifolds, N*M base manifolds and two electrode connecting bolts. The two electrode connecting bolts are arranged on the shell; the base is provided with the electrolyte ingress pipe and is connected with the base manifolds; the upper cover is provided with the electrolyte and gas delivery pipe and is connected with the upper cover manifolds; and four edges of the N+1 metal electrode plates are embedded in the upper cover, the shell and the base in equal distance, an electrolysis cell between every two metal electrode plates is communicated with the upper cover manifolds and the base manifolds which are evenly distributed, and the first and (N+1)th metal electrode plates are connected with the anode and the cathode of a power supply through the two electrode connecting bolts respectively. Because the manifolds have smaller diameters and are relatively long, the bypass parasitic current generated by the electrolyte flowing through the manifolds between the metal electrode plates is lower so as to reduce the loss and improve the electrolysis efficiency.
Description
Technical field
The utility model relates to a kind of high efficiency oxy-hydrogen electrolytic cell of the hydrogen and oxygen gas mixture that utilizes the brine electrolysis generation; hydrogen and oxygen atom are pressed 2: 1 accurate proportionings in the gas that brine electrolysis produces, and are used for the new energy technology of combustion engine energy-saving reduction of discharging and the field of environmental protection application technology.
Background technique
Along with world energy sources crisis and environmental issue become increasingly conspicuous, automotive industry is faced with stern challenge.On the one hand, the petroleum resources shortage, automobile is the oil consumption rich and influential family, and the thermal efficiency of present internal-combustion engine is lower, and the heat energy that fuel combustion produces approximately has only 35%-40% to be used for actual automobile running, and the automobile pollution that climbs up and up has aggravated this contradiction; On the other hand, a large amount of uses of automobile have aggravated environmental pollution, in the urban atmosphere 82% of CO, NOx 48%, 58% and the particulate of HC 8% from vehicle exhaust, in addition, a large amount of CO of motor vehicle emission
2Greenhouse effect have been aggravated.Therefore, energy-saving and emission-reduction have become the emphasis that various countries pay close attention to.
Many fuel-economizing products such as ozone injection, magnetic resonance etc. are arranged in the market, but effect is not clearly.And for example application number 200480040719.2, and complex structure also need be settled special radiating device on metal shell.Therefore the patent of invention of Wuhan Micro Hydrogen Technology Co., Ltd.'s application number is: 200810048766.1 " micro-hydrogen injection energy-saving exhaust-reduction device of internal combustion engine ", its simple in structure, reliable performance, but the oxy-hydrogen electrolytic cell in " micro-hydrogen injection energy-saving exhaust-reduction device of internal combustion engine " exists each metal electrode board to produce the bypass parasite current by 2 circulate electrolyte holes on the electrode plate, can not reach higher electrolytic efficiency.
Summary of the invention
The utility model provides a kind of high efficiency oxy-hydrogen electrolytic cell in order to overcome problem and the shortcoming that above-mentioned prior art exists, and the present invention changes circulate electrolyte by importing and derive the manifold realization.Because the diameter of manifold is very little and relatively very long, thus very little between each metal electrode board by the bypass parasite current that electrolytic solution produced in the manifold, thus reduced loss, improved electrolytic efficiency.
Technical solutions of the utility model are: 1, a kind of high efficiency oxy-hydrogen electrolytic cell, comprise housing, base, loam cake, N+1 metal electrode board, the electrolytic solution ingress pipe, electrolytic solution and gas eduction tube, N * M root loam cake manifold, N * M foundation seat manifold, two electrode connecting bolts, it is characterized in that: two electrode bolts are installed on the housing, base is provided with the electrolytic solution ingress pipe, the electrolytic solution ingress pipe links to each other with N * M foundation seat manifold, on be covered with electrolytic solution and gas eduction tube, electrolytic solution and gas eduction tube link to each other with N * M root loam cake manifold, 4 edges of N+1 metal electrode board are embedded in loam cake equidistantly, in housing and the base, electrolytic chamber between per two metal electrode boards is communicated with equally distributed loam cake manifold and base manifold, the 1st is connected the positive pole of power supply respectively with N+1 metal electrode board through two electrode connecting bolts, negative pole, wherein M is except that zero natural number, and N is for the natural number except that zero and be 6 multiple.
The utility model also comprises cell liquor pump, and cell liquor pump is installed in electrolytic solution and imports the mouth of pipe.
Described housing, base, loam cake are made by engineering plastics respectively.
Because no perforate and their 4 edges are embedded in base, loam cake and the housing of being made by engineering plastics equidistantly on N+1 the metal electrode board, form almost completely state of insulation.
Because NxM root manifold is with electrolytic solution ingress pipe, a N electrolytic chamber and electrolytic solution and the gas eduction tube correspondence is connected also and cell liquor pump forms the electrolytic solution vertical circulation, vertical current is through each electrolytic chamber from bottom to top for electrolytic solution, and the natural flow direction of the hydrogen-oxygen bubble that produces with brine electrolysis is consistent.Electrolytic solution constant speed each electrolytic chamber that flows through.Electrolytic solution washes away the metal electrode board surface continuously, cleaning impurity deposition.By the circulation of electrolytic solution, the heat of electrolytic cell is transferred to electrolytic etching of metal liquid liquid container.
The utlity model has following advantage: 1, electrolytic solution is shunted through manifold through the electrolytic solution ingress pipe that cell liquor pump pumps on the base again, flows into each electrolytic chamber, and the hydrogen and oxygen that produces together with electrolysis pumps through the electrolytic solution and the gas eduction tube of loam cake then.Because the diameter of manifold is very little and very long, so very little by the bypass parasite current that electrolytic solution produced in the manifold between each metal electrode board.Thereby reduced loss, improved electrolytic efficiency.The power consumpiton of every liter of oxyhydrogen gas of this electrolytic cell only is 2.5 watt-hours.2, since the electrolytic solution that pumps into stabilized speed each electrolytic chamber that flows through, and hydrogen, the oxygen bubbles of output carried out electrolytic chamber, overcome hydrogen, oxygen bubbles and attached to the drawback that the metal electrode board surface influences gas production, improved gas producing efficiency, and kept stable aerogenesis speed.3, metal electrode board is washed away continuously by electrolytic solution, settle accounts immediately the surface of metal electrode board, prevent from metal electrode board surface impurity deposition from progressively to reduce gas producing efficiency.4, the heat of electrolytic cell generation is transferred to the heat radiation of electrolytic solution metal storage tank by the circulation of electrolytic solution, makes the cell operation temperature reduce, and reduces the content of water vapor in the oxyhydrogen gas, has improved the quality of oxyhydrogen gas.
Description of drawings
Fig. 1 is a structural representation of the present utility model.
Embodiment
The utility model will be further described in conjunction with the accompanying drawings.
As shown in Figure 1, the present invention is by loam cake 1, base 2, housing 3,48 loam cake manifolds 4,48 foundation seat manifolds 5,13 metal electrode boards 6, two electrode connecting bolts 7, electrolytic solution ingress pipe 8, electrolytic solution and gas eduction tube 9, cell liquor pump 10 is formed, two electrode connecting bolts are installed on the housing with the 1st and the 13rd metal electrode board welding and sealing respectively, base 2 is provided with electrolytic solution ingress pipe 8 and links to each other with 48 foundation seat manifolds 5, cell liquor pump 10 is installed in 8 mouthfuls of electrolytic solution ingress pipes, loam cake 1 is provided with electrolytic solution and gas eduction tube 9 and links to each other with 48 loam cake manifolds 4,13 metal electrode boards 6 are embedded in the loam cake of being made by engineering plastics 1 equidistantly, in the accurate groove of base 2 and housing 3, form the good insulation between the metal electrode board; The electrolytic chamber 11 that forms between per two metal electrode boards 6 is communicated with equally distributed loam cake manifold 4 and base manifold 5 respectively, and 48 loam cake manifolds 4 and 48 foundation seat manifolds 5 evenly are arranged on loam cake 1 and the base 2.13 metal electrode boards 6 are formed a series connection electrolytic cell, and the 1st is connected the positive and negative electrode of power supply respectively with the 13rd metal electrode board 6 through electrode bolts 7.Through cell liquor pump 10, electrolytic solution ingress pipe 8, base manifold 5, electrolytic chamber 11, loam cake manifold 4, electrolytic solution and gas eduction tube 9 and blowback electrolyte liquid container, constitute a kind of constant current circulatory system from the electrolytic solution of electrolyte liquid container.
Insulation is inlayed by engineering plastics in four edges of the metal electrode board of electrolytic cell of the present utility model, and no circulate electrolyte hole on the metal electrode board makes each metal electrode board almost completely insulate.
Electrolytic solution pumps into electrolytic solution ingress pipe 8 on the base through cell liquor pump 10, again through 5 shuntings of base manifold, flow into each electrolytic chamber 11, the hydrogen and oxygen that produces together with electrolysis is pumped to electrolyte liquid container air-water separation by electrolytic solution and gas eduction tube 9 after loam cake manifold 4 compiles then. because the diameter of loam cake manifold and base manifold is very little and relative very long, thereby it is so very little between each metal electrode board by the bypass parasite current that electrolytic solution produced in the manifold. reduce power loss, improved electrolytic efficiency. the power consumpiton of every liter of oxyhydrogen gas of this electrolytic cell only is 2.5 watt-hours.
Because the electrolytic solution that pumps into is with constant speed each electrolytic chamber that flows through, and hydrogen, the oxygen bubbles of output carried out electrolytic chamber, overcome that hydrogen, oxygen bubbles attach to the metal electrode board surface and the drawback that influences gas production has improved gas producing efficiency, and kept stable aerogenesis speed.
Metal electrode board is washed away continuously by electrolytic solution, settle accounts immediately the surface of metal electrode board, prevent metal electrode board surface impurity deposition and progressively reduce the problem of gas producing efficiency.
The heat that electrolytic cell produces is transferred to the heat radiation of electrolyte metal tank by the circulation of electrolytic solution, makes the cell operation temperature reduce, and reduces the content of water vapor in the oxyhydrogen gas, has improved the quality of oxyhydrogen gas.
Claims (3)
1. high efficiency oxy-hydrogen electrolytic cell, comprise housing, base, loam cake, N+1 metal electrode board, the electrolytic solution ingress pipe, electrolytic solution and gas eduction tube, N * M root loam cake manifold, N * M foundation seat manifold, two electrode connecting bolts, it is characterized in that: two electrode connecting bolts are installed on the housing, base is provided with the electrolytic solution ingress pipe, the electrolytic solution ingress pipe links to each other with N * M foundation seat manifold, on be covered with electrolytic solution and gas eduction tube, electrolytic solution and gas eduction tube link to each other with N * M root loam cake manifold, 4 edges of N+1 metal electrode board are embedded in loam cake equidistantly, in housing and the base, electrolytic chamber between per two metal electrode boards is communicated with equally distributed loam cake manifold and base manifold, the 1st is connected the positive pole of power supply respectively with N+1 metal electrode board through two electrode connecting bolts, negative pole, wherein M is except that zero natural number, and N is for the natural number except that zero and be 6 multiple.
2. high efficiency oxy-hydrogen electrolytic cell according to claim 1 is characterized in that: comprise that also cell liquor pump, cell liquor pump are installed in electrolytic solution and import the mouth of pipe.
3. high efficiency oxy-hydrogen electrolytic cell according to claim 1 and 2 is characterized in that: described housing, base, loam cake are made by engineering plastics respectively.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200857809U CN201461148U (en) | 2009-05-15 | 2009-05-15 | Efficient oxy-hydrogen electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2009200857809U CN201461148U (en) | 2009-05-15 | 2009-05-15 | Efficient oxy-hydrogen electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN201461148U true CN201461148U (en) | 2010-05-12 |
Family
ID=42388502
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2009200857809U Expired - Lifetime CN201461148U (en) | 2009-05-15 | 2009-05-15 | Efficient oxy-hydrogen electrolytic bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN201461148U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105112935A (en) * | 2015-09-21 | 2015-12-02 | 李云飞 | Overpotential control structure and method |
| CN106048645A (en) * | 2016-07-14 | 2016-10-26 | 重庆大学 | Method for improving oxyhydrogen machine electric energy efficiency by external magnetic field |
-
2009
- 2009-05-15 CN CN2009200857809U patent/CN201461148U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105112935A (en) * | 2015-09-21 | 2015-12-02 | 李云飞 | Overpotential control structure and method |
| CN106048645A (en) * | 2016-07-14 | 2016-10-26 | 重庆大学 | Method for improving oxyhydrogen machine electric energy efficiency by external magnetic field |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20130723 Granted publication date: 20100512 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20140723 Granted publication date: 20100512 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PP01 | Preservation of patent right |
Effective date of registration: 20141020 Granted publication date: 20100512 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| PD01 | Discharge of preservation of patent |
Date of cancellation: 20150420 Granted publication date: 20100512 |
|
| RINS | Preservation of patent right or utility model and its discharge | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20161213 Address after: Wuhan University science and Technology Park of East Lake Development Zone Four Hubei Wu Da Yuan Road 430074 Wuhan City No. 9 Business Building 2 floor (East) Patentee after: Wuhan micro hydrogen new energy Co. Ltd. Address before: 430074 Wuhan science and Technology Industrial Park, East Lake Development Zone, Hubei, China Patentee before: Wuhan Weiqing Technology Co., Ltd. |
|
| CX01 | Expiry of patent term | ||
| CX01 | Expiry of patent term |
Granted publication date: 20100512 |