CN114635146B - Electrolytic tank structure for generating acidic electrolyzed oxidizing water - Google Patents
Electrolytic tank structure for generating acidic electrolyzed oxidizing water Download PDFInfo
- Publication number
- CN114635146B CN114635146B CN202210248311.4A CN202210248311A CN114635146B CN 114635146 B CN114635146 B CN 114635146B CN 202210248311 A CN202210248311 A CN 202210248311A CN 114635146 B CN114635146 B CN 114635146B
- Authority
- CN
- China
- Prior art keywords
- heat exchange
- clay block
- exchange sleeve
- electrolyzed oxidizing
- oxidizing 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.)
- Active
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 26
- 230000001590 oxidative effect Effects 0.000 title claims description 11
- 230000002378 acidificating effect Effects 0.000 title abstract description 17
- 239000004927 clay Substances 0.000 claims abstract description 23
- 229910052751 metal Inorganic materials 0.000 claims abstract description 17
- 239000002184 metal Substances 0.000 claims abstract description 17
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 13
- 230000003647 oxidation Effects 0.000 claims abstract description 12
- 239000012528 membrane Substances 0.000 claims abstract description 9
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 claims description 22
- 238000005868 electrolysis reaction Methods 0.000 claims description 18
- 238000011084 recovery Methods 0.000 claims description 11
- 210000005056 cell body Anatomy 0.000 claims description 9
- 210000004027 cell Anatomy 0.000 claims description 6
- 239000011248 coating agent Substances 0.000 claims description 6
- 238000000576 coating method Methods 0.000 claims description 6
- HCDGVLDPFQMKDK-UHFFFAOYSA-N hexafluoropropylene Chemical group FC(F)=C(F)C(F)(F)F HCDGVLDPFQMKDK-UHFFFAOYSA-N 0.000 claims description 6
- 238000010030 laminating Methods 0.000 claims description 5
- 229910001069 Ti alloy Inorganic materials 0.000 claims description 4
- UUWCBFKLGFQDME-UHFFFAOYSA-N platinum titanium Chemical compound [Ti].[Pt] UUWCBFKLGFQDME-UHFFFAOYSA-N 0.000 claims description 4
- XIUFWXXRTPHHDQ-UHFFFAOYSA-N prop-1-ene;1,1,2,2-tetrafluoroethene Chemical group CC=C.FC(F)=C(F)F XIUFWXXRTPHHDQ-UHFFFAOYSA-N 0.000 claims description 4
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 claims description 3
- 239000002253 acid Substances 0.000 claims description 2
- 230000004888 barrier function Effects 0.000 claims 3
- 238000005192 partition Methods 0.000 abstract description 9
- 239000004020 conductor Substances 0.000 description 19
- 239000000243 solution Substances 0.000 description 5
- 238000004064 recycling Methods 0.000 description 3
- 229910052802 copper Inorganic materials 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- -1 polytetrafluoroethylene Polymers 0.000 description 2
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 2
- 239000004810 polytetrafluoroethylene Substances 0.000 description 2
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- 102000004190 Enzymes Human genes 0.000 description 1
- 108090000790 Enzymes Proteins 0.000 description 1
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 230000004075 alteration Effects 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000000170 cell membrane Anatomy 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 239000000306 component Substances 0.000 description 1
- 239000008358 core component Substances 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000003792 electrolyte Substances 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 239000003014 ion exchange membrane Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000002503 metabolic effect Effects 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000033116 oxidation-reduction process Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 230000008961 swelling Effects 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B9/00—Cells or assemblies of cells; Constructional parts of cells; Assemblies of constructional parts, e.g. electrode-diaphragm assemblies; Process-related cell features
- C25B9/17—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof
- C25B9/19—Cells comprising dimensionally-stable non-movable electrodes; Assemblies of constructional parts thereof with diaphragms
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B1/00—Electrolytic production of inorganic compounds or non-metals
- C25B1/01—Products
- C25B1/02—Hydrogen or oxygen
- C25B1/04—Hydrogen or oxygen by electrolysis of water
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The invention discloses an electrolytic tank structure for generating acidic oxidation potential water, which comprises a metal tank body and a clay block lining, wherein the inner wall of the metal tank body is in fit connection with the clay block lining, a T-shaped seat is fixedly arranged at the bottom of an inner cavity of the clay block lining, an insulating partition plate and the T-shaped seat divide the inner cavity of the clay block lining into a left half electrolytic area and a right half electrolytic area, ion membrane plates are arranged in the left half electrolytic area and the right half electrolytic area, the two ion membrane plates are connected with the T-shaped seat, and cathode electrode plates are fixedly arranged on two sides of the insulating partition plate.
Description
Technical Field
The invention relates to an electrolytic tank structure, in particular to an electrolytic tank structure for generating acidic electrolyzed oxidizing water, and belongs to the technical field of electrolytic tanks.
Background
The electrolytic tank consists of a tank body, an anode and a cathode, and the anode chamber and the cathode chamber are separated by a diaphragm. The electrolyte is divided into three types, namely an aqueous solution electrolytic tank, a molten salt electrolytic tank and a nonaqueous solution electrolytic tank. When the direct current passes through the electrolytic cell, oxidation reaction occurs at the interface between the anode and the solution, and reduction reaction occurs at the interface between the cathode and the solution, so as to prepare the required product. The optimized design of the structure of the electrolytic tank and the reasonable selection of electrode and diaphragm materials are the keys for improving the current efficiency, reducing the tank voltage and saving the energy consumption.
The electrolytic bath is a key component and a core component of equipment for generating acidic oxidation potential water, and the working principle of the electrolytic bath is that softened tap water and a certain proportion of analytical pure NaCL solution are mixed by utilizing electrolytic reaction, and then are electrolyzed in the electrolytic bath containing an ion exchange membrane through a special platinum-titanium alloy electrode. The water coming out from one side of the anode is called acidic oxidation potential water, and the acidic oxidation potential water has the advantages of high sterilization speed, broad spectrum, safety, reliability, no residual toxicity, environmental protection and the like, and can damage the living environment of microorganisms, enhance the permeability of cell membranes, cause cell swelling, damage internal metabolic enzymes and enable the microorganisms to die rapidly due to the combined action of low pH value, high oxidation reduction potential and available chlorine.
However, when the conventional electrolytic tank is used, the conventional electrolytic tank is mostly matched with an anode and a cathode, the anode is supplied with current, the current flows back through the cathode, the electrolytic efficiency of the electrolytic tank is greatly reduced, the generation amount of acidic oxidation potential water is reduced, the generated heat cannot be recovered, and the heat in the exhaust gas and the acidic oxidation water level cannot be utilized, so that the storage is inconvenient.
Disclosure of Invention
The invention aims to provide an electrolytic cell structure for generating acidic electrolyzed oxidizing water, which solves the problems in the prior art.
In order to achieve the above purpose, the present invention provides the following technical solutions: the utility model provides a generate electrolysis trough structure of acid oxidation potential water, includes metal cell body and clay block inside lining, the inner wall and the laminating of clay block inside lining of metal cell body are connected, the bottom fixed mounting of clay block inside lining inner chamber has T type seat, the fixed insulating partition that is equipped with in middle part on T type seat top, insulating partition and T type seat divide into left half electrolysis district and right half electrolysis district with the inner chamber of clay block inside lining, the ion membrane board is all installed to the inside in left half electrolysis district and right half electrolysis district, two the ion membrane board all is connected with T type seat, the equal fixed mounting in both sides of insulating partition has the cathode electrode piece, the equal laminating in both sides of clay block inside lining inner chamber is connected with the anode electrode piece, the equal grafting in middle part of metal cell body both sides is connected with conductive terminal, two conductive terminal's one end all is connected with sealed insulating joint, two sealed insulating joint's one end all is connected with first pure copper wire, two the one end of first pure copper wire all is connected with the output end fixed connection of the integrated wiring end that is equipped with, the inside connection of two pure copper wire is equipped with hollow conductor, two hollow conductor and hollow conductor, two hollow conductor connected with two hollow conductor, two hollow conductor connected with hollow conductor, two hollow conductor connected with hollow conductor.
As a preferable technical scheme of the invention, the heat recovery structure comprises a heat shield body, wherein a first heat exchange sleeve and a second heat exchange sleeve are arranged in the heat shield body and are connected with corresponding hollow guide pipes in a sleeved mode, a first inlet pipe and a second inlet pipe are respectively arranged at one end of the first heat exchange sleeve and one end of the second heat exchange sleeve, and a converging pipeline is fixedly connected between the first heat exchange sleeve and the second heat exchange sleeve.
As a preferable technical scheme of the invention, the inner wall of the clay block lining is coated with a perfluoroethylene propylene coating, the perfluoroethylene propylene coating consists of tetrafluoroethylene and hexafluoropropylene, and the content of hexafluoropropylene is 10-15%.
As a preferable technical scheme of the invention, the anode electrode plate and the cathode electrode plate are platinum-titanium alloy electrodes.
As a preferred technical scheme of the invention, the wire current-carrying capacity of the second pure copper wire is twice that of the first pure copper wire.
As a preferred embodiment of the present invention, the heat exchange coefficient of the first heat exchange jacket is different from the heat exchange coefficient of the second heat exchange jacket.
As a preferable technical scheme of the invention, the top end of the metal groove body is buckled and connected with an insulating groove cover, and the middle part of the insulating groove cover is in sliding connection with the cathode electrode plate.
Compared with the prior art, the invention has the beneficial effects that:
1. according to the electrolytic tank structure for generating the acidic electrolyzed water, the metal tank body is divided into the left half electrolytic area and the right half electrolytic area through the T-shaped seat, the ion diaphragm plate and the insulating partition plate, the first pure copper wire and the second pure copper wire are used for respectively introducing current into the left half electrolytic area and the right half electrolytic area, and then the cathode electrode plate is used for forming a passage, so that the electrolytic efficiency of the electrolytic tank in unit time is greatly improved, the generation amount of the acidic electrolyzed water in unit time is improved, and the electrolytic tank structure is high in practicability.
2. The invention relates to an electrolytic tank structure for generating acidic oxidation potential water, which is provided with a heat shield body, a first heat exchange sleeve, a first inlet pipe, a second heat exchange sleeve, a converging pipe and a second inlet pipe, and is convenient for collecting discharged gas and recycling acidic oxidation water through a hollow pipe, wherein heat contained in the electrolytic tank structure is utilized through the first heat exchange sleeve and the second heat exchange sleeve, so that the heat is convenient to recycle, the heat recycling efficiency is improved, and the use is convenient.
Drawings
FIG. 1 is a schematic diagram of the structure of the present invention;
FIG. 2 is a schematic view of the internal structure of the heat shield body of the present invention.
In the figure: 1. a metal tank body; 2. a clay block liner; 3. a power plug; 4. a second pure copper wire; 5. an integrated terminal block; 6. a first pure copper wire; 7. sealing the insulating joint; 8. a conductive contact; 9. an anode electrode sheet; 10. a T-shaped seat; 11. an ion membrane plate; 12. an insulating separator; 13. a cathode electrode sheet; 14. an integrated plug; 15. an insulating slot cover; 16. a hollow conduit; 17. a heat shield body; 18. a first heat exchange jacket; 19. a first inlet pipe; 20. a second heat exchange jacket; 21. a confluence pipe; 22. and a second inlet pipe.
Detailed Description
The following description of the embodiments of the present invention will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
Referring to fig. 1-2, the invention provides a technical scheme of an electrolytic cell structure for generating acidic electrolyzed oxidizing water, which comprises the following steps:
according to the illustration of fig. 1-2, including metal cell body 1 and clay block inside lining 2, the inner wall of metal cell body 1 is connected with the laminating of clay block inside lining 2, the bottom fixed mounting of clay block inside lining 2 inner chamber has T type seat 10, the middle part on T type seat 10 top is fixed to be equipped with insulating partition 12, insulating partition 12 and T type seat 10 divide into left half electrolysis district and right half electrolysis district with the inner chamber of clay block inside lining 2, ion membrane plate 11 is all installed to the inside in left half electrolysis district and right half electrolysis district, two ion membrane plates 11 all are connected with T type seat 10, the equal fixed mounting in both sides of insulating partition 12 has cathode electrode piece 13, the equal laminating in both sides of clay block inside lining 2 inner chamber is connected with anode electrode piece 9, the middle part of metal cell body 1 both sides is all pegged graft and is connected with conductive connection, the one end of two conductive connection 8 all is connected with sealed insulating connection 7, the one end of two sealed insulating connection 7 all is connected with first pure copper wire 6, the one end of two first pure copper wire 6 all is connected with the output fixed connection of integrated terminal 5 that is equipped with, the inside connection terminal 5, the two hollow conductor 16 is equipped with two hollow conductor 16 and is connected with two hollow conductor 16, two hollow conductor 16 inside hollow conductor 16 are connected with two hollow conductor 16, two hollow conductor 16 are connected with the inside hollow conductor 16 and two hollow conductor 16 are connected with the inside hollow conductor 16.
According to the embodiment shown in fig. 1 and 2, the heat recovery structure comprises a heat-insulating cover body 17, a first heat exchange sleeve 18 and a second heat exchange sleeve 20 are installed in the heat-insulating cover body 17, the first heat exchange sleeve 18 and the second heat exchange sleeve 20 are sleeved and connected with corresponding hollow guide pipes 16, a first inlet pipe 19 and a second inlet pipe 22 are installed at one end of the first heat exchange sleeve 18 and one end of the second heat exchange sleeve 20 respectively, a confluence pipeline 21 is fixedly connected between the first heat exchange sleeve 18 and the second heat exchange sleeve 20, heat recovery is facilitated, heat recovery is improved, a polytetrafluoroethylene coating is coated on the inner wall of a clay liner 2, the polytetrafluoroethylene coating consists of tetrafluoroethylene and hexafluoropropylene, the hexafluoropropylene content is 10-15%, an anode electrode plate 9 and a cathode electrode plate 13 are platinum-titanium alloy electrodes, good conductive performance and good service life are achieved, the wire flow of a second pure copper wire 4 is twice that of a first pure copper wire 6, the heat exchange coefficient of the first heat exchange sleeve 18 and the second heat exchange sleeve 20 are not good, the heat recovery effect is improved, the heat recovery is achieved by a metal groove cover 1 is connected with a heat recovery groove cover, the heat recovery effect is improved, and a metal groove cover 1 is connected with the heat recovery groove cover is provided.
When the invention is used, the anode electrode plate 9 is supplied with current, the first pure copper lead 6 and the second pure copper lead 4 are respectively used for supplying current to the insides of the left half electrolysis area and the right half electrolysis area, and then the cathode electrode plate 13 is used for forming a passage, so that the electrolysis efficiency of the electrolytic cell in unit time is greatly improved, the generation amount of acidic oxidation potential water in unit time is improved, the practicability is high, the discharged gas is conveniently collected and the acidic oxidation water is conveniently recycled through the two hollow guide pipes 16, and the contained heat is conveniently recycled through the first heat exchange sleeve 18 and the second heat exchange sleeve 20, thereby improving the heat recycling efficiency and being convenient to use.
In the description of the present invention, it should be understood that the orientation or positional relationship indicated is based on the orientation or positional relationship shown in the drawings, and is merely for convenience in describing the present invention and simplifying the description, and does not indicate or imply that the apparatus or element referred to must have a specific orientation, be configured and operated in a specific orientation, and thus should not be construed as limiting the present invention.
In the present invention, unless explicitly specified and defined otherwise, for example, it may be fixedly connected, detachably connected, or integrally formed; can be mechanically or electrically connected; either directly or indirectly through intermediaries, or in communication with each other or in interaction with each other, unless explicitly defined otherwise, the meaning of the terms described above in this application will be understood by those of ordinary skill in the art in view of the specific circumstances.
Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made therein without departing from the principles and spirit of the invention, the scope of which is defined in the appended claims and their equivalents.
Claims (7)
1. The utility model provides a generate electrolytic tank structure of acid oxidation potential water, includes metal cell body (1) and clay block inside lining (2), its characterized in that, the inner wall and the clay block inside lining (2) laminating of metal cell body (1) are connected, the bottom fixed mounting of clay block inside lining (2) inner chamber has T type seat (10), the middle part at T type seat (10) top is fixed to be equipped with insulating barrier (12), insulating barrier (12) and T type seat (10) divide into left half electrolysis district and right half electrolysis district with the inner chamber of clay block inside lining (2), ion membrane board (11) are all installed to the inside of left half electrolysis district and right half electrolysis district, two ion membrane board (11) all are connected with T type seat (10), the both sides of insulating barrier (12) all fixed mounting have negative pole electrode piece (13), the both sides of clay block inside lining (2) inner chamber all are laminated and are connected with positive pole electrode piece (9), the middle part all in both sides of metal cell body (1) is connected with conducting connection (8), two conducting connection has conducting wire (6) in the middle part of both sides, two conducting connection (7) are all connected with one end (6) of a sealed connection wire (6) and one end (6) are all connected with one end (6) of pure copper wire (6) respectively, the integrated terminal head (5) is connected with a second pure copper wire (4), one end fixedly connected with power plug (3) of second pure copper wire (4), two the one end of negative pole electrode piece (13) all with integrated plug (14) fixed connection that are equipped with, the inside in half electrolysis district in left side and the inside in half electrolysis district in right side all communicate there is hollow pipe (16), two hollow pipe (16) all are connected with the heat recovery structure that is equipped with.
2. An electrolyzer structure for generating electrolyzed oxidizing water according to claim 1, characterized in that: the heat recovery structure comprises a heat shield body (17), a first heat exchange sleeve (18) and a second heat exchange sleeve (20) are mounted in the heat shield body (17), the first heat exchange sleeve (18) and the second heat exchange sleeve (20) are sleeved with corresponding hollow pipes (16) to be connected, a first inlet pipe (19) and a second inlet pipe (22) are mounted at one end of the first heat exchange sleeve (18) and one end of the second heat exchange sleeve (20) respectively, and a converging pipeline (21) is fixedly connected between the first heat exchange sleeve (18) and the second heat exchange sleeve (20).
3. An electrolyzer structure for generating electrolyzed oxidizing water according to claim 1, characterized in that: the inner wall of the clay block lining (2) is coated with a perfluoroethylene propylene coating, the perfluoroethylene propylene coating consists of tetrafluoroethylene and hexafluoropropylene, and the content of the hexafluoropropylene is 10-15%.
4. An electrolyzer structure for generating electrolyzed oxidizing water according to claim 1, characterized in that: the anode electrode plate (9) and the cathode electrode plate (13) are platinum-titanium alloy electrodes.
5. An electrolyzer structure for generating electrolyzed oxidizing water according to claim 1, characterized in that: the wire current-carrying capacity of the second pure copper wire (4) is twice that of the first pure copper wire (6).
6. An electrolytic cell structure for generating electrolyzed oxidizing water according to claim 2, wherein: the heat exchange coefficient of the first heat exchange jacket (18) is different from the heat exchange coefficient of the second heat exchange jacket (20).
7. An electrolyzer structure for generating electrolyzed oxidizing water according to claim 1, characterized in that: the top of the metal groove body (1) is buckled and connected with an insulating groove cover (15), and the middle part of the insulating groove cover (15) is in sliding connection with the cathode electrode plate (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210248311.4A CN114635146B (en) | 2022-03-14 | 2022-03-14 | Electrolytic tank structure for generating acidic electrolyzed oxidizing water |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202210248311.4A CN114635146B (en) | 2022-03-14 | 2022-03-14 | Electrolytic tank structure for generating acidic electrolyzed oxidizing water |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN114635146A CN114635146A (en) | 2022-06-17 |
| CN114635146B true CN114635146B (en) | 2024-01-09 |
Family
ID=81947904
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202210248311.4A Active CN114635146B (en) | 2022-03-14 | 2022-03-14 | Electrolytic tank structure for generating acidic electrolyzed oxidizing water |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN114635146B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07236888A (en) * | 1994-02-28 | 1995-09-12 | Nippon Intec Kk | Electrolytic water and oxidation potential water making apparatus |
| JPH07328639A (en) * | 1994-06-02 | 1995-12-19 | Nippon Intec Kk | Oxidation potential water forming device |
| CN104562092A (en) * | 2015-02-03 | 2015-04-29 | 奉新赣锋锂业有限公司 | Multi-anode lithium metal electrolytic bath |
| CN206680226U (en) * | 2017-03-27 | 2017-11-28 | 长春云卫科技有限公司 | Acidic oxidized electric potential water produces electrolytic cell |
| CN211734057U (en) * | 2019-12-21 | 2020-10-23 | 武汉丽辉新技术有限公司 | Acidic oxidation potential water generator |
| CN212246339U (en) * | 2020-05-08 | 2020-12-29 | 河北宏泰丰业医疗器械有限公司 | Electrolytic tank of acidic oxidation potential water generator |
| CN213803049U (en) * | 2020-11-06 | 2021-07-27 | 江西坤灿环保科技股份有限公司 | Acidic electrolytic tank |
| CN214936277U (en) * | 2021-06-25 | 2021-11-30 | 石首市金祥米业有限公司 | Acidic oxidation potential water generating device |
-
2022
- 2022-03-14 CN CN202210248311.4A patent/CN114635146B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH07236888A (en) * | 1994-02-28 | 1995-09-12 | Nippon Intec Kk | Electrolytic water and oxidation potential water making apparatus |
| JPH07328639A (en) * | 1994-06-02 | 1995-12-19 | Nippon Intec Kk | Oxidation potential water forming device |
| CN104562092A (en) * | 2015-02-03 | 2015-04-29 | 奉新赣锋锂业有限公司 | Multi-anode lithium metal electrolytic bath |
| CN206680226U (en) * | 2017-03-27 | 2017-11-28 | 长春云卫科技有限公司 | Acidic oxidized electric potential water produces electrolytic cell |
| CN211734057U (en) * | 2019-12-21 | 2020-10-23 | 武汉丽辉新技术有限公司 | Acidic oxidation potential water generator |
| CN212246339U (en) * | 2020-05-08 | 2020-12-29 | 河北宏泰丰业医疗器械有限公司 | Electrolytic tank of acidic oxidation potential water generator |
| CN213803049U (en) * | 2020-11-06 | 2021-07-27 | 江西坤灿环保科技股份有限公司 | Acidic electrolytic tank |
| CN214936277U (en) * | 2021-06-25 | 2021-11-30 | 石首市金祥米业有限公司 | Acidic oxidation potential water generating device |
Non-Patent Citations (1)
| Title |
|---|
| "酸性氧化电位水制备技术研究进展";余浩 等;《中国消毒学杂志》;第155-158页 * |
Also Published As
| Publication number | Publication date |
|---|---|
| CN114635146A (en) | 2022-06-17 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101721860B1 (en) | Method for the cogeneration of electrical and hydrogen power | |
| US20040197649A1 (en) | Load leveling battery and methods therefor | |
| CN113913844B (en) | Power switching-based membrane-free water electrolysis hydrogen production device | |
| CN101956206B (en) | Electrolytic device and technology for preparing hydrogen and oxygen through seawater electrolysis | |
| CN113862690B (en) | Water electrolysis hydrogen production device based on bipolar electrode system | |
| CN114635146B (en) | Electrolytic tank structure for generating acidic electrolyzed oxidizing water | |
| CN103165961A (en) | Tandem-type underwater metal/oxygen cell stack | |
| CN109680293A (en) | A kind of half electrolytic water device of single reaction electrode | |
| WO2018079965A1 (en) | Hybrid power generation system and energy-independent hydrogen-electricity hybrid charging station, which use reverse electrodialysis device capable of efficiently producing hydrogen-electricity | |
| CN104862730A (en) | Method for preparing potassium permanganate through ion-membrane electrolysis and special electrolytic bath applied to same | |
| CN210176966U (en) | Hydrogen-rich water generating device based on aluminum-air battery | |
| US7914934B2 (en) | Hydro-oxy fuel generator | |
| WO2003017407A1 (en) | Improved load leveling battery and methods therefor | |
| JPH0938653A (en) | Production of electrolyzed ionic water and device therefor | |
| CN114068995B (en) | All-iron oxidation flow battery system | |
| CN221166770U (en) | Hydrogen production water electrolysis tank with good sealing performance | |
| WO2015101914A1 (en) | Apparatus for producing hydrogen using sea water without evolution of chlorine and method thereof | |
| CN213113534U (en) | Novel electrolytic water tank | |
| JP2007059196A (en) | Power generating system | |
| CN208430239U (en) | A kind of electrolyzer electric pole insulating nut | |
| CN219280053U (en) | Multipole type electrolytic device for producing hydrogen peroxide and hydrogen by electrolyzing ammonium bisulfate | |
| CN221028701U (en) | Gas preparation system | |
| CN219861610U (en) | Anode end plate based on PEM water electrolysis tank | |
| CN215771293U (en) | Metal-acid-hydrogen energy battery | |
| CN114108015B (en) | Filter-pressing type membraneless water electrolytic tank |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| PB01 | Publication | ||
| PB01 | Publication | ||
| SE01 | Entry into force of request for substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant |