CN212581571U - Electrolytic bath - Google Patents
Electrolytic bath Download PDFInfo
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- CN212581571U CN212581571U CN202020989881.5U CN202020989881U CN212581571U CN 212581571 U CN212581571 U CN 212581571U CN 202020989881 U CN202020989881 U CN 202020989881U CN 212581571 U CN212581571 U CN 212581571U
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- shell
- diaphragm
- polar plates
- electrolytic cell
- plates
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Abstract
The utility model provides an electrolytic cell, which comprises a shell, wherein one end of the shell is provided with a mixed liquid inlet, the other end of the shell is provided with an electrolytic solution outlet, a separation frame is arranged in the shell, a plurality of groups of channel structures are arranged in the separation frame, and two ends of the separation frame are fixed through screws; the diaphragm and the polar plate are arranged in each channel structure of the partition frame, the sealing rings are further arranged at two ends of each channel structure, the polar plates and the diaphragms in the channel structures are arranged alternately to form a structure separated by the diaphragms between the polar plates, one side of each diaphragm and the adjacent polar plates form an anode chamber, the other side of each diaphragm and the adjacent polar plates form a cathode chamber, the pipeline structure is removed, the partition frames are used between the polar plates, the diaphragms are separated, the polar plates are sealed by the sealing rings, the polar plates and the shell are filled with environment-friendly resin, and the sealing performance is better.
Description
Technical Field
The utility model relates to a functional water electrolysis equipment, concretely relates to electrolytic cell.
Background
The electrolytic cell is configured to generate an acidic solution at an anode of the electrolytic cell and an alkaline solution at a cathode of the electrolytic cell by electrolyzing an electrolytic solution (drinking water or water to which an electrolyte is added).
The traditional electrolytic cell has the advantages of small electrolytic range, small water treatment amount and strong limitation, and the splicing mode of the pipeline adopts planar flange connection, so that the sealing property of the joint is poor, and the safety of a production workshop is threatened. And the electrode plates in the electrolytic cell are easy to scale, which affects the service life of the electrode plates.
Disclosure of Invention
In order to overcome the defects in the prior art, the utility model provides an electrolytic cell, which has removed the pipeline structure, uses a separation frame between a polar plate and the polar plate, separates a diaphragm, is sealed by a sealing ring, and is filled with environment-friendly resin between the polar plate group and a shell, so that the sealing property is better.
In order to achieve the purpose, the electrolytic cell comprises a shell, wherein one end of the shell is provided with a mixed liquid inlet, the other end of the shell is provided with an electrolytic solution outlet, a partition frame is arranged in the shell, a plurality of groups of channel structures are arranged in the partition frame, and two ends of the partition frame are fixed through screws; the diaphragm and the polar plate are arranged in each channel structure of the partition frame, the sealing rings are further arranged at two ends of each channel structure, the polar plates and the diaphragms in the channel structures are arranged alternately to form a structure that the polar plates are separated from the polar plates by the diaphragms, one side of each diaphragm and the adjacent polar plates form an anode chamber, and the other side of each diaphragm and the adjacent polar plates form a cathode chamber.
Further, a resin layer is arranged between the separation frame and the shell.
Furthermore, the polar plate is arranged on one side of the channel structure and fixed at two ends of the separation frame through the screw, and the diaphragm is arranged on the separation frame in the middle of the channel structure.
Furthermore, a wiring copper bar is arranged outside the shell.
Further, the polar plate is a titanium metal polar plate.
Further, the diaphragm is a ceramic nano diaphragm.
The utility model provides an electrolytic cell: 1. the pipeline structure is removed, the polar plates are separated from each other by the partition frame and the diaphragm and then sealed by the sealing ring, and the polar plate group and the shell are filled with environment-friendly resin, so that the sealing property is better.
2. The combination has strong variability, and the multiple parallel combination can be carried out on the number of the pole plates of the electrolytic cell by calculation according to the requirements of customers, thereby meeting the requirements of different customers on water treatment capacity.
3. The positive and negative electrodes can be switched at will. By inverting the electrode, the scaling of the electrode plate in the electrolytic cell can be prevented, the service life of the electrode plate is prolonged, the time and the cost are effectively saved for customers, and the production efficiency is improved.
Drawings
FIG. 1 is a sectional elevation view of the electrolytic cell of the present invention;
FIG. 2 is a top view of the electrolytic cell of the present invention;
FIG. 3 is a side sectional structural view of the electrolytic cell of the present invention;
FIG. 4 is an electrolytic schematic diagram of the electrolytic cell of the utility model;
reference numerals: the electrolytic cell comprises a shell 1, a mixed liquid inlet 2, an electrolytic solution outlet 3, a separation frame 4, a channel structure 5, a screw rod 6, a diaphragm 7, a polar plate 8, a sealing ring 9, an anode chamber 10, a cathode chamber 11, a resin layer 12 and a wiring copper bar 13.
Detailed Description
The technical solution of the present invention will be more clearly and completely explained by the description of the preferred embodiments of the present invention with reference to the accompanying drawings.
As shown in fig. 1 to 3, the electrolytic cell of the present invention comprises a casing 1, one end of the casing 1 is provided with a mixed liquid inlet 2, the other end is provided with an electrolytic solution outlet 3, a partition frame 4 is arranged in the casing 1, a plurality of sets of channel structures 5 are arranged in the partition frame, and two ends of the partition frame are fixed by screws 6; the diaphragm 7 and the polar plate 8 are arranged in each channel structure of the partition frame, the sealing rings 9 are further arranged at two ends of each channel structure, the polar plates and the diaphragms in the channel structures are arranged alternately to form a structure that the polar plates are separated from each other by the diaphragms, one side of each diaphragm and the adjacent polar plates form an anode chamber 10, and the other side of each diaphragm and the adjacent polar plates form a cathode chamber 11.
A resin layer 12 is also arranged between the shelf and the shell.
The polar plates are arranged on one side of the channel structure and fixed at two ends of the separation frame through screws, and the diaphragm is arranged on the separation frame in the middle of the channel structure.
And a wiring copper bar 13 is also arranged outside the shell.
The polar plate is a titanium metal polar plate.
The diaphragm is a ceramic nanometer diaphragm.
When the mixed solution enters the tank, electrolysis occurs, negative ions move to the positive electrode of the electrode, and positive ions move to the negative electrode of the electrode. The partition frame guides the flow of the solution, and the solution is finally divided into acidic liquid and alkaline liquid to be discharged. As shown in figure 4, the utility model discloses the electrolysis trough theory of operation: when the two polar plates are connected with a direct current power supply, the solution is injected into the groove by pressure to generate ionization, and the generated anions and cations selectively pass through the ceramic nanometer diaphragm and enter the anode chamber and the cathode chamber under the action of an electric field. Finally, an acidic solution is produced in the anode chamber and an alkaline solution is produced in the cathode chamber; the generated acidic solution or alkaline solution can be discharged through an electrolytic solution outlet (the positions of the sealing rings arranged at the two ends of the adjusting channel structure), and acid or alkaline solutions with different PH values and different concentrations are generated through electrolysis; such as to produce a hypochlorous acid solution.
The utility model provides an electrolytic bath, removed pipeline structure, with the shelf that separates between polar plate and the polar plate, the diaphragm separation is sealed by the sealing washer again, packs with environmental protection resin between polar plate group and the shell, and the leakproofness is better.
Claims (6)
1. An electrolytic cell comprises a shell, wherein one end of the shell is provided with a mixed liquid inlet, and the other end of the shell is provided with an electrolytic solution outlet; the diaphragm and the polar plate are arranged in each channel structure of the partition frame, the sealing rings are further arranged at two ends of each channel structure, the polar plates and the diaphragms in the channel structures are arranged alternately to form a structure that the polar plates are separated from the polar plates by the diaphragms, one side of each diaphragm and the adjacent polar plates form an anode chamber, and the other side of each diaphragm and the adjacent polar plates form a cathode chamber.
2. An electrolytic cell according to claim 1 wherein a resin layer is further disposed between the frame and the shell.
3. An electrolytic cell according to claim 1 wherein the plates are disposed on one side of the channel structure and secured at either end of the spacer by screws, and the diaphragm is disposed on the spacer in the middle of the channel structure.
4. The electrolytic cell of claim 1 wherein the housing is further externally provided with a copper wiring bar.
5. An electrolytic cell according to claim 1 wherein said plates are titanium metal plates.
6. An electrolytic cell according to claim 1 wherein the membrane is a microporous nano-membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020989881.5U CN212581571U (en) | 2020-06-03 | 2020-06-03 | Electrolytic bath |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202020989881.5U CN212581571U (en) | 2020-06-03 | 2020-06-03 | Electrolytic bath |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN212581571U true CN212581571U (en) | 2021-02-23 |
Family
ID=74642775
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202020989881.5U Active CN212581571U (en) | 2020-06-03 | 2020-06-03 | Electrolytic bath |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN212581571U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022213693A1 (en) * | 2021-04-07 | 2022-10-13 | 湖南满缘红水科技有限公司 | Low-salt eow electrolytic tank, low-salt eow electrolytic device, and low-salt eow preparation method |
-
2020
- 2020-06-03 CN CN202020989881.5U patent/CN212581571U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2022213693A1 (en) * | 2021-04-07 | 2022-10-13 | 湖南满缘红水科技有限公司 | Low-salt eow electrolytic tank, low-salt eow electrolytic device, and low-salt eow preparation method |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20230803 Address after: Room 113, Management Committee of Panlong New Area, Beishe Village, Panlong Town, Jintai District, Baoji City, Shaanxi Province, 721000 Patentee after: Shaanxi Ruichengda New Material Technology Co.,Ltd. Address before: 721000 Liangquan Industrial Park, Maying Town, high tech Development Zone, Baoji City, Shaanxi Province Patentee before: Baoji Ruicheng Titanium Industry Co.,Ltd. |
|
| TR01 | Transfer of patent right |