CN204738030U - Effectual no diaphragm electrolysis groove of electrolysis - Google Patents
Effectual no diaphragm electrolysis groove of electrolysis Download PDFInfo
- Publication number
- CN204738030U CN204738030U CN201520448863.5U CN201520448863U CN204738030U CN 204738030 U CN204738030 U CN 204738030U CN 201520448863 U CN201520448863 U CN 201520448863U CN 204738030 U CN204738030 U CN 204738030U
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- China
- Prior art keywords
- electrolysis
- coated steel
- steel sheet
- electrolytic zinc
- electrolyzer
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- 238000005868 electrolysis reaction Methods 0.000 title claims abstract description 54
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 32
- 230000015572 biosynthetic process Effects 0.000 claims abstract description 4
- 229910000831 Steel Inorganic materials 0.000 claims description 79
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 claims description 79
- 239000010959 steel Substances 0.000 claims description 79
- 239000011701 zinc Substances 0.000 claims description 79
- 229910052725 zinc Inorganic materials 0.000 claims description 79
- 238000007789 sealing Methods 0.000 claims description 4
- 239000000463 material Substances 0.000 claims description 3
- 229910001220 stainless steel Inorganic materials 0.000 claims description 3
- 239000010935 stainless steel Substances 0.000 claims description 3
- 239000000203 mixture Substances 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 5
- 235000020188 drinking water Nutrition 0.000 abstract description 2
- 239000003651 drinking water Substances 0.000 abstract description 2
- 230000007306 turnover Effects 0.000 abstract 2
- 239000008399 tap water Substances 0.000 description 13
- 235000020679 tap water Nutrition 0.000 description 13
- 210000004027 cell Anatomy 0.000 description 11
- 230000004888 barrier function Effects 0.000 description 4
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 3
- 239000012267 brine Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 210000005056 cell body Anatomy 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 discloses an effectual no diaphragm electrolysis groove of electrolysis, including electrolysis trough upper cover, electrolysis board and electrolysis trough bottom plate, the electrolysis board is a plurality of altogether, and stacks in proper order between electrolysis trough upper cover and electrolysis trough bottom plate, covers on the electrolysis trough to be equipped with 2 business turn over water adapters, be equipped with the paddle hole on the electrolysis board, the paddle hole is totally 2, and corresponding with 2 business turn over water adapter positions respectively, the electrolysis board comprises electrolysis board A, electrolysis board B and plate electrode, and the plate electrode includes negative pole and positive pole, and negative pole and positive pole all are the slice, and it is flat -plate -shaped that flaky negative pole and flaky positive pole separate the range constitution each other, and electrolysis board A and electrolysis board B mutually support at the snakelike basin of both inside formation, and the plate electrode is located between electrolysis board A and the electrolysis board B, and installs in the basin, this electrolysis trough, the drinking water is when electrolysis inboard mobile, flow time is longer, at the in -process that flows, do not stop by the plate electrode electrolysis, therefore the electrolysis is effectual.
Description
Technical field
The utility model relates to a kind of electrolyzer, the undivided cell that specifically a kind of electrolysis effectiveness is good.
Background technology
Electrolyzer is conventional electrolyzer.Along with the development in epoch, electrolyzer range of application extend to drinking-water water field, carries out the rich hydrogen water of electrolytic preparation, drink rich hydrogen water and be conducive to the healthy of people by electrolyzer to tap water.Electrolyzer is in the market made up of cell body, anode and negative electrode, and use barrier film to be separated in anolyte compartment and cathode compartment, barrier film adds the cost of electrolyzer.When rich hydrogen water prepared by electrolytic tank electrolysis tap water in the market in addition, the time that tap water flows through electrolyzer is shorter, causes the electrolysis effectiveness of electrolyzer not good.
Utility model content
The purpose of this utility model is the undivided cell providing a kind of electrolysis effectiveness good, to solve the problem proposed in above-mentioned background technology.
For achieving the above object, the utility model provides following technical scheme:
The undivided cell that electrolysis effectiveness is good, comprises electrolyzer upper cover, electrolytic zinc-coated steel sheet and electrolyzer base plate; Described electrolytic zinc-coated steel sheet is multiple altogether, and overlays between electrolyzer upper cover and electrolyzer base plate successively; Described electrolyzer covers and is provided with 2 Inlet and outlet water adapters; Described electrolytic zinc-coated steel sheet is provided with paddle hole, paddle hole totally 2, be respectively paddle hole A and paddle hole B, paddle hole A and paddle hole B are corresponding with 2 Inlet and outlet water adapter positions respectively, the Inlet and outlet water adapter that electrolyzer covers is connected with the paddle hole on the electrolytic zinc-coated steel sheet near electrolyzer upper cover, and the paddle hole on adjacent 2 electrolytic zinc-coated steel sheets is connected; Described electrolytic zinc-coated steel sheet is made up of electrolytic zinc-coated steel sheet A, electrolytic zinc-coated steel sheet B and the battery lead plate between electrolytic zinc-coated steel sheet A and electrolytic zinc-coated steel sheet B, battery lead plate comprises negative electrode and anode, negative electrode and anode are all in the form of sheets, the negative electrode of sheet and the spaced arrangement of the anode of sheet form tabular, electrolytic zinc-coated steel sheet A and electrolytic zinc-coated steel sheet B cooperatively interacts at the snakelike tank of both inner formation, battery lead plate between electrolytic zinc-coated steel sheet A and electrolytic zinc-coated steel sheet B, and is arranged in tank.
As further program of the utility model: the quantity of described electrolytic zinc-coated steel sheet can superpose arbitrarily.
As the utility model further scheme: be provided with sealing plate between described electrolyzer base plate and the electrolytic zinc-coated steel sheet near electrolyzer base plate.
As the utility model further scheme: 2 Inlet and outlet water adapters are located at the diagonally opposing corner two ends of electrolyzer upper cover respectively, and Inlet and outlet water adapter is also furnished with corresponding fixed plate.
As the utility model further scheme: the Inlet and outlet water adapter that described electrolyzer covers and be provided with gasket near between the paddle hole on the electrolytic zinc-coated steel sheet of electrolyzer upper cover, and be also provided with gasket between paddle hole on adjacent 2 electrolytic zinc-coated steel sheets.
As the utility model further scheme: described negative electrode and anode are strip-shaped blade.
As the utility model further scheme: the material of described electrolyzer base plate is stainless steel.
Compared with prior art, the beneficial effects of the utility model are: 1, do not have barrier film in this electrolyzer, reduce the cost of manufacture of electrolyzer; 2, this electrolyzer, during the flowing of tap water in electrolytic zinc-coated steel sheet, need to flow to the other end from one end of the snakelike tank in electrolytic zinc-coated steel sheet, in flow process, ceaselessly by battery lead plate electrolysis, flowing time is longer, therefore electrolysis effectiveness is good, and in addition because this electrolyzer is provided with multiple electrolytic zinc-coated steel sheet, multiple electrolytic zinc-coated steel sheet works simultaneously and carries out brine electrolysis, therefore electrolytic efficiency is higher, can't affect electrolytic efficiency because tap water residence time in electrolytic zinc-coated steel sheet is long.
Accompanying drawing explanation
Fig. 1 is the structural representation of the undivided cell that electrolysis effectiveness is good.
Fig. 2 is the structural representation of electrolytic zinc-coated steel sheet in the undivided cell that electrolysis effectiveness is good.
Fig. 3 is that in the undivided cell that electrolysis effectiveness is good, electrolytic zinc-coated steel sheet takes off the structural representation after electrolytic zinc-coated steel sheet A.
In figure: 1-fixed plate, 2-Inlet and outlet water adapter, 3-electrolyzer upper cover, 4-gasket, 5-electrolytic zinc-coated steel sheet, 51-electrolytic zinc-coated steel sheet A, 52-battery lead plate, 53-electrolytic zinc-coated steel sheet B, 54-paddle hole A, 55-paddle hole B, 6-sealing plate, 7-electrolyzer base plate.
Embodiment
Below in conjunction with the accompanying drawing in the utility model embodiment, be clearly and completely described the technical scheme in the utility model embodiment, obviously, described embodiment is only the utility model part embodiment, instead of whole embodiments.Based on the embodiment in the utility model, those of ordinary skill in the art are not making the every other embodiment obtained under creative work prerequisite, all belong to the scope of the utility model protection.
Refer to Fig. 1 ~ 3, in the utility model embodiment, the undivided cell that a kind of electrolysis effectiveness is good, comprises electrolyzer upper cover 3, electrolytic zinc-coated steel sheet 5 and electrolyzer base plate 7, described electrolytic zinc-coated steel sheet 5 is multiple altogether, and overlay between electrolyzer upper cover 3 and electrolyzer base plate 7 successively, preferably, the quantity of described electrolytic zinc-coated steel sheet 5 can superpose arbitrarily, be provided with sealing plate 6 between electrolyzer base plate 7 and the electrolytic zinc-coated steel sheet 5 near electrolyzer base plate 7, the material of described electrolyzer base plate 7 is stainless steel, described electrolyzer upper cover 3 is provided with 2 Inlet and outlet water adapters 2, preferably, 2 Inlet and outlet water adapters 2 are located at the diagonally opposing corner two ends of electrolyzer upper cover 3 respectively, Inlet and outlet water adapter 2 is also furnished with corresponding fixed plate 1, one of them Inlet and outlet water adapter 2 is as water supply connector, and another is as water out adapter, described electrolytic zinc-coated steel sheet 5 is provided with paddle hole, paddle hole totally 2, be respectively paddle hole A 54 and paddle hole B 55, paddle hole A 54 and paddle hole B 55 are corresponding with 2 Inlet and outlet water adapter 2 positions respectively, Inlet and outlet water adapter 2 on electrolyzer upper cover 3 is connected with near the paddle hole on the electrolytic zinc-coated steel sheet 5 of electrolyzer upper cover 3, and the paddle hole on adjacent 2 electrolytic zinc-coated steel sheets 5 is connected, Inlet and outlet water adapter 2 on described electrolyzer upper cover 3 and be provided with gasket 4 near between the paddle hole on the electrolytic zinc-coated steel sheet 5 of electrolyzer upper cover 3, and be also provided with gasket 4 between paddle hole on adjacent 2 electrolytic zinc-coated steel sheets 5, described electrolytic zinc-coated steel sheet 5 is by electrolytic zinc-coated steel sheet A 51, electrolytic zinc-coated steel sheet B 53, and the battery lead plate 52 between electrolytic zinc-coated steel sheet A 51 and electrolytic zinc-coated steel sheet B 53 forms, battery lead plate 52 comprises negative electrode and anode, negative electrode and anode are all in the form of sheets, the negative electrode of sheet and the spaced arrangement of the anode of sheet form tabular, electrolytic zinc-coated steel sheet A 51 and electrolytic zinc-coated steel sheet B 53 cooperatively interacts at the snakelike tank of both inner formation, battery lead plate 52 is between electrolytic zinc-coated steel sheet A 51 and electrolytic zinc-coated steel sheet B53, and be arranged in tank, tap water enters after in electrolytic zinc-coated steel sheet 5, the other end is flow to from one end of snakelike tank, in flow process, ceaselessly by battery lead plate 52 electrolysis, flowing time is longer, therefore electrolysis effectiveness is good, preferably, described negative electrode and anode are strip-shaped blade.
Principle of work of the present utility model is: the undivided cell that described electrolysis effectiveness is good, tap water enters electrolyzer from one of them Inlet and outlet water adapter 2, this Inlet and outlet water adapter 2 is as water supply connector, after tap water enters electrolyzer from water supply connector, enter in each electrolytic zinc-coated steel sheet 5 by paddle hole, the tap water entered in electrolytic zinc-coated steel sheet 5 flow to water out adapter by another paddle hole on electrolytic zinc-coated steel sheet 5, and then flows out.During the flowing of tap water in electrolytic zinc-coated steel sheet 5, need to flow to the other end from one end of the snakelike tank in electrolytic zinc-coated steel sheet 5, in flow process, ceaselessly by battery lead plate 52 electrolysis, flowing time is longer, and therefore electrolysis effectiveness is good.Because this electrolyzer is provided with multiple electrolytic zinc-coated steel sheet 5, multiple electrolytic zinc-coated steel sheet 5 works simultaneously and carries out brine electrolysis, and therefore electrolytic efficiency is higher, can't affect electrolytic efficiency because tap water residence time in electrolytic zinc-coated steel sheet 5 is long.
There is no barrier film in the undivided cell that described electrolysis effectiveness is good, reduce the cost of manufacture of electrolyzer; The undivided cell that described electrolysis effectiveness is good, during the flowing of tap water in electrolytic zinc-coated steel sheet 5, need to flow to the other end from one end of the snakelike tank in electrolytic zinc-coated steel sheet 5, in flow process, ceaselessly by battery lead plate 52 electrolysis, flowing time is longer, therefore electrolysis effectiveness is good, and in addition because this electrolyzer is provided with multiple electrolytic zinc-coated steel sheet 5, multiple electrolytic zinc-coated steel sheet 5 works simultaneously and carries out brine electrolysis, therefore electrolytic efficiency is higher, can't affect electrolytic efficiency because tap water residence time in electrolytic zinc-coated steel sheet 5 is long.
To those skilled in the art, obvious the utility model is not limited to the details of above-mentioned one exemplary embodiment, and when not deviating from spirit of the present utility model or essential characteristic, can realize the utility model in other specific forms.Therefore, no matter from which point, all should embodiment be regarded as exemplary, and be nonrestrictive, scope of the present utility model is limited by claims instead of above-mentioned explanation, and all changes be therefore intended in the implication of the equivalency by dropping on claim and scope are included in the utility model.Any Reference numeral in claim should be considered as the claim involved by limiting.
In addition, be to be understood that, although this specification sheets is described according to embodiment, but not each embodiment only comprises an independently technical scheme, this narrating mode of specification sheets is only for clarity sake, those skilled in the art should by specification sheets integrally, and the technical scheme in each embodiment also through appropriately combined, can form other embodiments that it will be appreciated by those skilled in the art that.
Claims (7)
1. the undivided cell that electrolysis effectiveness is good, is characterized in that, comprises electrolyzer upper cover (3), electrolytic zinc-coated steel sheet (5) and electrolyzer base plate (7), described electrolytic zinc-coated steel sheet (5) is multiple altogether, and overlays between electrolyzer upper cover (3) and electrolyzer base plate (7) successively, described electrolyzer upper cover (3) is provided with 2 Inlet and outlet water adapters (2), described electrolytic zinc-coated steel sheet (5) is provided with paddle hole, paddle hole totally 2, be respectively paddle hole A (54) and paddle hole B (55), paddle hole A (54) and paddle hole B (55) are corresponding with 2 Inlet and outlet water adapter (2) positions respectively, Inlet and outlet water adapter (2) on electrolyzer upper cover (3) is connected with near the paddle hole on the electrolytic zinc-coated steel sheet (5) of electrolyzer upper cover (3), and the paddle hole on adjacent 2 electrolytic zinc-coated steel sheets (5) is connected, described electrolytic zinc-coated steel sheet (5) is by electrolytic zinc-coated steel sheet A (51), electrolytic zinc-coated steel sheet B (53), and battery lead plate (52) composition be positioned between electrolytic zinc-coated steel sheet A (51) and electrolytic zinc-coated steel sheet B (53), battery lead plate (52) comprises negative electrode and anode, negative electrode and anode are all in the form of sheets, the negative electrode of sheet and the spaced arrangement of the anode of sheet form tabular, electrolytic zinc-coated steel sheet A (51) and electrolytic zinc-coated steel sheet B (53) cooperatively interacts at the snakelike tank of both inner formation, battery lead plate (52) is positioned between electrolytic zinc-coated steel sheet A (51) and electrolytic zinc-coated steel sheet B (53), and be arranged in tank.
2. the undivided cell that electrolysis effectiveness according to claim 1 is good, is characterized in that, the quantity of described electrolytic zinc-coated steel sheet (5) can superpose arbitrarily.
3. the undivided cell that electrolysis effectiveness according to claim 1 and 2 is good, it is characterized in that, between described electrolyzer base plate (7) and the electrolytic zinc-coated steel sheet (5) near electrolyzer base plate (7), be provided with sealing plate (6).
4. the undivided cell that electrolysis effectiveness according to claim 3 is good, it is characterized in that, 2 Inlet and outlet water adapters (2) are located at the diagonally opposing corner two ends of electrolyzer upper cover (3) respectively, and Inlet and outlet water adapter (2) is also furnished with corresponding fixed plate (1).
5. the undivided cell that the electrolysis effectiveness according to claim 1 or 2 or 4 is good, it is characterized in that, Inlet and outlet water adapter (2) on described electrolyzer upper cover (3) and be provided with gasket (4) near between the paddle hole on the electrolytic zinc-coated steel sheet (5) of electrolyzer upper cover (3), and be also provided with gasket (4) between paddle hole on adjacent 2 electrolytic zinc-coated steel sheets (5).
6. the undivided cell that electrolysis effectiveness according to claim 1 is good, is characterized in that, described negative electrode and anode are strip-shaped blade.
7. the undivided cell that electrolysis effectiveness according to claim 1 is good, is characterized in that, the material of described electrolyzer base plate (7) is stainless steel.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520448863.5U CN204738030U (en) | 2015-06-26 | 2015-06-26 | Effectual no diaphragm electrolysis groove of electrolysis |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520448863.5U CN204738030U (en) | 2015-06-26 | 2015-06-26 | Effectual no diaphragm electrolysis groove of electrolysis |
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| Publication Number | Publication Date |
|---|---|
| CN204738030U true CN204738030U (en) | 2015-11-04 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520448863.5U Active CN204738030U (en) | 2015-06-26 | 2015-06-26 | Effectual no diaphragm electrolysis groove of electrolysis |
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105755502A (en) * | 2016-05-10 | 2016-07-13 | 东莞市升瑞资环保科技有限公司 | Multi-variable combined multifunctional electrolytic bath |
| CN106757122A (en) * | 2015-11-23 | 2017-05-31 | 上海好旭新能源科技发展有限公司 | For electrolysis water without spacing diaphragm-free electrolysis device |
| CN106995927A (en) * | 2016-01-25 | 2017-08-01 | 吾土产业株式会社 | Skin rejuvenation equipment |
| CN114381745A (en) * | 2022-01-17 | 2022-04-22 | 上海喜运环保科技有限公司 | Electrolytic generator module based on zigzag flow channel formed by multilayer electrode combination |
-
2015
- 2015-06-26 CN CN201520448863.5U patent/CN204738030U/en active Active
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106757122A (en) * | 2015-11-23 | 2017-05-31 | 上海好旭新能源科技发展有限公司 | For electrolysis water without spacing diaphragm-free electrolysis device |
| CN106995927A (en) * | 2016-01-25 | 2017-08-01 | 吾土产业株式会社 | Skin rejuvenation equipment |
| CN105755502A (en) * | 2016-05-10 | 2016-07-13 | 东莞市升瑞资环保科技有限公司 | Multi-variable combined multifunctional electrolytic bath |
| CN114381745A (en) * | 2022-01-17 | 2022-04-22 | 上海喜运环保科技有限公司 | Electrolytic generator module based on zigzag flow channel formed by multilayer electrode combination |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20210903 Address after: 510700 rooms 401 and 402, building 6, No. 188, Kaiyuan Avenue, Huangpu District, Guangzhou, Guangdong Patentee after: Guangzhou Songsheng Technology Co.,Ltd. Address before: 523000 No. 182, Kwai Qing Road, Qinghuang village, Qingxi Town, Dongguan City, Guangdong Province Patentee before: DONGGUAN SONGSHENG ELECTRONIC TECHNOLOGY Co.,Ltd. |
|
| CP03 | Change of name, title or address | ||
| CP03 | Change of name, title or address |
Address after: Room 801, Building 1, No. 8 Luoyongfang Industrial Second Road, Wanjiang Street, Dongguan City, Guangdong Province, 523000 Patentee after: Guangdong Songsheng Technology Co.,Ltd. Address before: 510700 rooms 401 and 402, building 6, No. 188, Kaiyuan Avenue, Huangpu District, Guangzhou, Guangdong Patentee before: Guangzhou Songsheng Technology Co.,Ltd. |