CN219670222U - Modularized electrochemical water treatment device - Google Patents
Modularized electrochemical water treatment device Download PDFInfo
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- CN219670222U CN219670222U CN202320233936.3U CN202320233936U CN219670222U CN 219670222 U CN219670222 U CN 219670222U CN 202320233936 U CN202320233936 U CN 202320233936U CN 219670222 U CN219670222 U CN 219670222U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 48
- 238000011282 treatment Methods 0.000 title claims abstract description 31
- 238000005868 electrolysis reaction Methods 0.000 claims abstract description 26
- 230000009347 mechanical transmission Effects 0.000 claims abstract description 9
- 238000003466 welding Methods 0.000 claims abstract description 4
- 230000005540 biological transmission Effects 0.000 claims description 7
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 16
- 238000011418 maintenance treatment Methods 0.000 abstract description 2
- 238000001514 detection method Methods 0.000 abstract 1
- 239000010865 sewage Substances 0.000 description 10
- 239000002351 wastewater Substances 0.000 description 7
- 239000000498 cooling water Substances 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 3
- BVKZGUZCCUSVTD-UHFFFAOYSA-M Bicarbonate Chemical compound OC([O-])=O BVKZGUZCCUSVTD-UHFFFAOYSA-M 0.000 description 2
- VTYYLEPIZMXCLO-UHFFFAOYSA-L Calcium carbonate Chemical compound [Ca+2].[O-]C([O-])=O VTYYLEPIZMXCLO-UHFFFAOYSA-L 0.000 description 2
- 230000002378 acidificating effect Effects 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 238000003487 electrochemical reaction Methods 0.000 description 2
- 230000005686 electrostatic field Effects 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 150000002500 ions Chemical class 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000004065 wastewater treatment Methods 0.000 description 2
- BHPQYMZQTOCNFJ-UHFFFAOYSA-N Calcium cation Chemical compound [Ca+2] BHPQYMZQTOCNFJ-UHFFFAOYSA-N 0.000 description 1
- JLVVSXFLKOJNIY-UHFFFAOYSA-N Magnesium ion Chemical compound [Mg+2] JLVVSXFLKOJNIY-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910000019 calcium carbonate Inorganic materials 0.000 description 1
- 229910001424 calcium ion Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 230000005764 inhibitory process Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- VTHJTEIRLNZDEV-UHFFFAOYSA-L magnesium dihydroxide Chemical compound [OH-].[OH-].[Mg+2] VTHJTEIRLNZDEV-UHFFFAOYSA-L 0.000 description 1
- 239000000347 magnesium hydroxide Substances 0.000 description 1
- 229910001862 magnesium hydroxide Inorganic materials 0.000 description 1
- 229910001425 magnesium ion Inorganic materials 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000000737 periodic effect Effects 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model discloses a modularized electrochemical water treatment device which is characterized by comprising six modules, namely an electrolysis chamber module, a pollution discharge chamber module, an anode module, a cathode module, a mechanical transmission module and a junction box module; the electrolysis chamber module is positioned right above the pollution discharge chamber module, and the whole equipment is formed by adopting a splicing or welding mode; anode modules and cathode modules are alternately arranged and positioned on the water inlet side of the electrolysis chamber module; the mechanical transmission module is positioned at the center of the water inlet side of the electrolysis chamber module; the junction box module is located directly above the anode module and the cathode module. When the module is failed or damaged, the module can be quickly disassembled, assembled and repaired by replacing the corresponding standardized module; when the anode module or the cathode module is damaged, the single anode module or the cathode module can be independently disassembled and assembled according to the detection and positioning damage positions, so that convenient independent maintenance treatment is realized, the disassembly and damage to other parts are avoided in the replacement process, and the device is a standardized green energy-saving water treatment device for each component.
Description
Technical Field
The utility model relates to the technical field of water treatment, in particular to a modularized electrochemical water treatment device.
Background
The electrochemical water treatment technology is broken through and developed continuously, plays an important role in the field of sewage and wastewater treatment, is particularly used as one of the technical means of descaling and scale inhibition in a circulating cooling water system, converts consumed electric energy into chemical energy, generates oxidation-reduction reaction on the surfaces of an anode and a cathode, forms acidic substances in an anode region, can reduce the alkalinity in the circulating cooling water system, and consumes bicarbonate ions in the circulating cooling water system by a method of forming a large amount of scales of calcium carbonate, magnesium hydroxide and the like in the cathode region, so that the alkalinity in the circulating cooling water system is further reduced; through the electrochemical reaction of the anode and the cathode, calcium ions and magnesium ions are removed, and part of bicarbonate ions are removed, so that the concentration of scale forming ions in the circulating cooling water system is reduced, the scale formation risk of the circulating cooling water system is reduced, the usage amount of acidic agents of the system can be reduced, and the introduction of ions and the pollution of other water bodies are reduced.
In the electrochemical water treatment device in the prior art, a method of connecting parts such as an anode, a cathode and a transmission in series is generally adopted, or the anode and the cathode adopt a technical method of integrally connecting in series and parallel, so that once the electrochemical water treatment device has local faults, damaged parts can be replaced only by completing a large amount of disassembly work, electrode surface damage easily occurs in the disassembly and assembly work process of the electrochemical water treatment device, potential safety hazards exist in the operation process, the mechanical fault rate is continuously improved, and the service life and the safety stability of the electrochemical water treatment device are seriously influenced.
Aiming at the above situation, how to realize convenient independent maintenance treatment, the disassembly and damage to other parts are avoided in the replacement process, and each component is a standardized green energy-saving water treatment device, which is an important research task.
Disclosure of Invention
Aiming at the problems in the technical background, the utility model aims to provide the modularized electrochemical water treatment device, which can solve the technical problems that once the electrochemical water treatment device in the prior art has local faults, a great deal of damaged parts are required to be disassembled and replaced, electrode damage occurs in the disassembling and assembling working process, potential safety hazards exist in the running process, the mechanical fault rate is high, and the service life and the safety stability of the electrochemical water treatment device are seriously influenced.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the modularized electrochemical water treatment device is characterized by comprising six modules, namely an electrolysis chamber module, a pollution discharge chamber module, an anode module, a cathode module, a mechanical transmission module and a junction box module; the electrolysis chamber module is positioned right above the pollution discharge chamber module, and the whole equipment is formed by adopting a splicing or welding mode; the anode modules and the cathode modules are alternately arranged and positioned on the water inlet side of the electrolysis chamber module; the mechanical transmission module is positioned at the center of the water inlet side of the electrolysis chamber module; the junction box module is located directly above the anode module and the cathode module.
Further, the electrolytic chamber module comprises a water inlet, a water outlet, a fixed groove, an overflow plate and an adjusting plate.
Further, the blowdown chamber module comprises a first blowdown outlet, a second blowdown outlet, a ground supporting plate, a longitudinal dividing beam and a transverse dividing beam.
Further, the anode module comprises an electrolysis anode, an anode fixing plate I, an anode fixing plate II and an anode fixing bolt.
Further, the cathode module comprises an electrolytic cathode, a first cathode fixing plate, a second cathode fixing plate and a cathode fixing bolt.
Further, the mechanical transmission module comprises a first scaler, a second scaler, a central shaft and a transmission shaft.
Further, the junction box module is an integrally preformed module.
Due to the adoption of the technical scheme, the utility model has at least the following technical effects or advantages:
(1) The electrolytic chamber module and the pollution discharge chamber module adopt a production technology method of independent modules, and form a whole by a splicing or welding method, so that the problem that the pollution discharge chamber is partially replaced when seriously damaged in actual use is solved, and the shell of the whole device is not replaced;
(2) The anode module adopts a standardized part production technical method, so that the anode modules of the same type of electrochemical water treatment devices have the same technical parameters, and adopts a method of opposite close splicing, thereby being beneficial to solving the problem that anodes generated in actual use cannot be independently disassembled and replaced, and the electrolytic anode adopts a flat plate-shaped or three-dimensional net-shaped structure, so that the sewage and the wastewater can be subjected to oxidation reaction on the surface of the anode with high efficiency;
(3) The cathode module adopts a standardized part production technical method, so that the anode modules of the electrochemical water treatment devices of the same model have the same technical parameters, and adopts a method of opposite close splicing, which is beneficial to solving the problem that the cathodes in actual use cannot be independently disassembled and replaced;
the modularized electrochemical water treatment device has the advantages of compact structure and reasonable design, can quickly realize the disassembly, assembly and maintenance of parts of the device, reduces the potential safety hazard existing in the operation process of the device, reduces the mechanical failure rate, prolongs the service life and safety stability of the electrochemical water treatment device, adopts various high-standardization modules, is a standardized module assembly technical route, and can be widely applied to the purification treatment of sewage and wastewater.
Drawings
FIG. 1 is a schematic view of a modular electrochemical water treatment apparatus of the present utility model;
FIG. 2 is a schematic view of the structure of the electrolytic cell module of the present utility model;
FIG. 3 is a schematic view of a trapway module according to the present utility model;
FIG. 4 is a schematic view of the structure of an anode module according to the present utility model;
FIG. 5 is a schematic view of a cathode module according to the present utility model;
FIG. 6 is a schematic view of a mechanical module according to the present utility model;
in the figure, 10-electrolytic cell module; 1001-water inlet; 1002-a water outlet; 1003-a fixed groove; 1004-an overflow plate; 1005-adjusting plate; 11-a blowdown chamber module; 1101-first drain outlet; 1102-a second sewage outlet; 1103-floor support plate; 1104-longitudinally dividing the beam; 1105-transverse dividing beams; 12-an anode module; 1201-electrolysis anode; 1202-anode fixing plate one; 1203-anode fixing plate two; 1204-anode fixing bolts; 13-a cathode module; 1301-electrolysis cathode; 1302-cathode fixing plate one; 1303-cathode fixing plate II; 1304-cathode fixing bolts; 14-a mechanical module; 1401-first scaler; 1402-second scaler; 1403-central axis; 1404-a drive shaft; 15-a power motor; 16-module fixing plate I; 17-a second module fixing plate; 18-a module fixing plate III; 19-a mechanical fixing plate; 20-junction box module.
Detailed Description
The following examples are illustrative of the utility model but are not intended to limit the utility model. The technical means used in the examples are conventional methods unless otherwise specified. The consumables referred to in the examples are commercially available unless otherwise specified.
Referring to fig. 1 to 6, a modularized electrochemical water treatment device comprises six modules, namely an electrolysis chamber module 10, a pollution discharge chamber module 11, an anode module 12, a cathode module 13, a mechanical transmission module 14 and a junction box module 20;
the electrolytic chamber module 10 comprises a water inlet 1001, a water outlet 1002, a fixed groove 1003, an overflow plate 1004 and an adjusting plate 1005; the plurality of water inlets 1001 and water outlets 1002 are respectively arranged, and sewage and wastewater are uniformly distributed into the electrolysis chamber module 10 through the plurality of water inlets 1001, so that sewage and wastewater enter a gap area formed by a plurality of groups of anode modules 12 and cathode modules 13, a certain electrostatic field exists in the gap area, the electrostatic field intensity is related to the minimum distance between the electrolysis anode 1201 and the electrolysis cathode 1301, the smaller the distance is, the smaller the gap area volume is, and the larger the pollutant concentration drop amplitude after sewage and wastewater treatment is; after the sewage and wastewater are subjected to electrochemical reaction treatment, the sewage and wastewater flows out from the opposite gap area formed by the anode module 12 and the cathode module 13, flows out from the hollow area of the second module fixing plate 17, flows out from the hollow area of the second module fixing plate through the adjusting plate 1005 to control the flow rate and the liquid level of the sewage and wastewater, flows into the other side of the electrolysis chamber module 10 across the overflow plate 1004, and finally flows out from the plurality of water outlets 1002.
The pollution discharge chamber module 11 comprises a first pollution discharge port 1001, a second pollution discharge port 1002, a ground supporting plate 1003, a longitudinal dividing beam 1004 and a transverse dividing beam 1005, the dirt adsorbed on the surface of the electrolytic cathode 1301 is removed by the rotation of the first cleaner 1401 and the second cleaner 1402, a part of the dirt is deposited in the area near the first pollution discharge port 1001 through the longitudinal dividing beam 1004 under the action of gravity, the other part of the dirt is deposited in the area near the second pollution discharge port 1002 through the longitudinal dividing beam 1004 under the action of gravity before flowing out of the device, and the first pollution discharge port 1001 and the second pollution discharge port 1002 discharge the dirt in the pollution discharge chamber module 11 through periodic pollution discharge.
The mechanical module 14 comprises a first cleaner 1401, a second cleaner 1402, a central shaft 1403 and a transmission shaft 1404, wherein the transmission shaft 1404 is matched with the power motor 15, the rotation parameters of the power motor 15 are regulated and controlled by a control system, the power motor 15 drives the transmission shaft 14 to move, the transmission shaft 14 drives the central shaft 1403 to move, the first cleaner 1401 and the second cleaner 1402 are fixed on the central shaft 1403 and move along with the central shaft 1403, and the support of the central shaft 1403 is positioned at the position of a central hole of the mechanical fixing plate 19.
The anode module 12 comprises an electrolysis anode 1201, an anode fixing plate 1202, an anode fixing plate 1203 and an anode fixing bolt 1204, wherein the electrolysis anode 1201 is positioned at the middle position of the anode fixing plate 1202 and the anode fixing plate 1203 and is fixedly connected into a whole through the anode fixing bolt 1204.
The cathode module 13 includes an electrolytic cathode 1301, a first cathode fixing plate 1302, a second cathode fixing plate 1303, and a cathode fixing bolt 1304, where the electrolytic cathode 1301 is located in the middle of the first cathode fixing plate 1302 and the second cathode fixing plate 1303, and is fixedly connected to form a whole through the cathode fixing bolt 1304.
The anode modules 12 and the cathode modules 13 are closely and alternately arranged, the number of single groups of the anode modules 12 is n, the number of single groups of the cathode modules 13 is m, and the total number of the anode modules 12 and the cathode modules 13 which are closely and alternately arranged in the electrolysis chamber module 10 is two groups, and the two groups are in mirror image relationship, so that in the electrolysis chamber module 10, the total number of the anode modules 12 is 2n, and the total number of the cathode modules 13 is 2 m.
The anode module 12 and the cathode module 13 are tightly arranged, four corners are tightly connected by a module fixing plate III 18, the middle area is tightly connected by a module fixing plate I16 and a module fixing plate II 17, the top is connected with a junction box module 20, when the anode module 12 or the cathode module 13 needs to be disassembled and assembled, the anode module 12 or the cathode module 13 is independently disassembled and assembled according to the position, if the anode module is positioned in the middle area, the first module fixing plate 16 or the second module fixing plate 17 is taken out, the wiring terminal of the electrode in the junction box module 20 is disassembled, the anode module 12 or the cathode module 13 moves along the horizontal direction and then moves along the vertical direction, the modules are independently taken out from the electrolytic chamber module 10, the order is opposite during installation, the modules firstly move along the vertical direction and then move along the horizontal direction, and finally the wiring terminal of the electrode is installed, so that the module disassembly work is conveniently and rapidly completed, and other modules are not damaged or affected.
The foregoing has shown and described the principal features of the utility model and the advantages of the utility model. It will be understood by those skilled in the art that the present utility model is not limited to the above-described embodiments, and that the above-described embodiments and the description are merely basic design principles of the present utility model, and that various changes and modifications may be made therein without departing from the spirit and scope of the utility model, which is defined in the appended claims. The scope of the utility model is defined by the appended claims and equivalents thereof.
Claims (7)
1. The modularized electrochemical water treatment device is characterized by comprising six modules, namely an electrolysis chamber module, a pollution discharge chamber module, an anode module, a cathode module, a mechanical transmission module and a junction box module; the electrolysis chamber module is positioned right above the pollution discharge chamber module, and the whole equipment is formed by adopting a splicing or welding mode; the anode modules and the cathode modules are alternately arranged and positioned on the water inlet side of the electrolysis chamber module; the mechanical transmission module is positioned at the center of the water inlet side of the electrolysis chamber module; the junction box module is located directly above the anode module and the cathode module.
2. A modular electrochemical water treatment apparatus as claimed in claim 1, wherein the electrolysis chamber module comprises a water inlet, a water outlet, a fixed tank, an overflow plate, and a regulating plate.
3. A modular electrochemical water treatment apparatus as claimed in claim 1, wherein the trapway module comprises a trapway one, a trapway two, a floor support plate, a longitudinal dividing beam, a transverse dividing beam.
4. A modular electrochemical water treatment apparatus as claimed in claim 1, wherein the anode module comprises an electrolysis anode, an anode fixing plate one, an anode fixing plate two, and an anode fixing bolt.
5. A modular electrochemical water treatment apparatus as claimed in claim 1, wherein the cathode module comprises an electrolytic cathode, a first cathode fixing plate, a second cathode fixing plate, and a cathode fixing bolt.
6. A modular electrochemical water treatment apparatus according to claim 1, wherein the mechanical transmission module comprises a first scaler, a second scaler, a central shaft, and a transmission shaft.
7. A modular electrochemical water treatment apparatus as claimed in claim 1, wherein the junction box module is a unitary prefabricated module.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320233936.3U CN219670222U (en) | 2023-02-16 | 2023-02-16 | Modularized electrochemical water treatment device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202320233936.3U CN219670222U (en) | 2023-02-16 | 2023-02-16 | Modularized electrochemical water treatment device |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN219670222U true CN219670222U (en) | 2023-09-12 |
Family
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202320233936.3U Active CN219670222U (en) | 2023-02-16 | 2023-02-16 | Modularized electrochemical water treatment device |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN219670222U (en) |
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2023
- 2023-02-16 CN CN202320233936.3U patent/CN219670222U/en active Active
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