CN210856356U - High-efficient electrolysis trough for chemical industry - Google Patents
High-efficient electrolysis trough for chemical industry Download PDFInfo
- Publication number
- CN210856356U CN210856356U CN201921368326.4U CN201921368326U CN210856356U CN 210856356 U CN210856356 U CN 210856356U CN 201921368326 U CN201921368326 U CN 201921368326U CN 210856356 U CN210856356 U CN 210856356U
- Authority
- CN
- China
- Prior art keywords
- electrolytic cell
- telescopic rod
- plate
- electric telescopic
- shell
- 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
- 239000000126 substance Substances 0.000 title claims abstract description 16
- 238000005868 electrolysis reaction Methods 0.000 title claims description 23
- 238000006243 chemical reaction Methods 0.000 claims abstract description 40
- 238000003756 stirring Methods 0.000 claims abstract description 14
- 238000001816 cooling Methods 0.000 claims abstract description 12
- 239000000110 cooling liquid Substances 0.000 claims abstract description 7
- 239000007788 liquid Substances 0.000 claims description 6
- 239000000463 material Substances 0.000 claims description 5
- 239000002826 coolant Substances 0.000 claims description 4
- 238000003889 chemical engineering Methods 0.000 claims description 2
- 238000000034 method Methods 0.000 abstract description 4
- 230000002035 prolonged effect Effects 0.000 abstract description 3
- 239000003792 electrolyte Substances 0.000 description 6
- 230000017525 heat dissipation Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 238000004519 manufacturing process Methods 0.000 description 2
- CTSLXHKWHWQRSH-UHFFFAOYSA-N oxalyl chloride Chemical compound ClC(=O)C(Cl)=O CTSLXHKWHWQRSH-UHFFFAOYSA-N 0.000 description 2
- 230000036632 reaction speed Effects 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000002146 bilateral effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 238000013021 overheating Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000006479 redox reaction Methods 0.000 description 1
Images
Landscapes
- Electrolytic Production Of Metals (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
The utility model relates to the technical field of electrolytic cells for chemical industry, in particular to a high-efficiency electrolytic cell for chemical industry, which comprises an electrolytic cell shell and a cooling box, wherein the electrolytic cell shell is arranged inside the cooling box, the electrolytic cell shell is connected with a cover plate, the cover plate is provided with a first reaction plate, a second reaction plate and a motor, the motor is provided with a stirring shaft, the electrolytic cell shell is provided with a first electric telescopic rod machine and a second electric telescopic rod machine, the first electric telescopic rod machine and the second electric telescopic rod machine are both provided with telescopic rods, each telescopic rod is provided with a hairbrush plate, the electrolytic cell shell is provided with a limiting chute, the electrolytic cell shell is provided with a plurality of radiating fins, the cooling box is provided with a transfusion tube, the transfusion tube is provided with a pump machine, the cooling box and the inside of the transfusion tube are provided with cooling liquid, the high-efficiency electrolytic cell for chemical industry has simple structure, the service life is prolonged, and the method is suitable for popularization.
Description
Technical Field
The utility model relates to an electrolysis trough technical field for the chemical industry especially relates to an electrolysis trough for high-efficient chemical industry.
Background
The electrolysis is a process of passing current through an electrolyte solution or a molten electrolyte to cause redox reaction on a cathode and an anode, an electrochemical cell can generate an electrolysis process when direct current voltage is applied, an electrolytic tank is often used as an electrolytic medium in the production of oxalyl chloride, the traditional electrolytic tank is complex to operate, heat cannot be timely dissipated in the electrolysis process, great trouble is brought to the electrolytic use of chemical materials, an electrolytic plate is inconvenient to fix, the electrolyte is not easy to flow, so that the full electrolysis cannot be realized, the quality of an electrolyzed product cannot be guaranteed, the electrolysis efficiency is low, and the production requirement of the chemical materials cannot be met, so that the high-efficiency electrolytic tank for chemical engineering is provided.
SUMMERY OF THE UTILITY MODEL
The utility model aims at solving the defects of low electrolysis efficiency and poor heat dissipation effect in the prior art and providing an electrolytic cell for high-efficiency chemical industry.
In order to achieve the above purpose, the utility model adopts the following technical scheme:
the utility model provides a design high-efficient electrolysis trough for chemical industry, including electrolysis trough shell and cooler bin, the electrolysis trough shell is established inside the cooler bin, the top of electrolysis trough shell is connected with the apron through the buckle, the symmetry is equipped with first reaction plate and second reaction plate on the apron, the apron outside is equipped with the motor, the output of motor is equipped with the (mixing) shaft, the both ends symmetry of (mixing) shaft is equipped with the bearing, the bilateral symmetry of electrolysis trough shell is equipped with first electric telescopic handle machine and second electric telescopic handle machine, the output of first electric telescopic handle machine and second electric telescopic handle machine all is equipped with the telescopic link, all be equipped with the brush board on every telescopic link, the inboard symmetry of electrolysis trough shell is equipped with spacing spout, the telescopic link is located spacing spout, the outer wall of electrolysis trough shell is equipped with a plurality of radiating fin, the top of cooler bin is equipped with the transfer line, be equipped with the pump machine.
Preferably, the first reaction plate and the second reaction plate are provided with through holes which are uniformly distributed at equal intervals.
Preferably, the stirring shaft is provided with cross rods distributed at equal intervals, the brush plate is provided with hard bristles, and the brush plate, the hard bristles and the stirring shaft are all in an inert material structure.
Preferably, the radiating fins are of a grid structure, are uniformly distributed on the outer wall of the shell of the electrolytic cell at equal intervals, and are fully immersed in the cooling liquid.
The utility model provides a pair of high-efficient electrolysis trough for chemical industry, beneficial effect lies in: the stirring shaft is driven to rotate by the motor, so that the electrolyte in the shell of the electrolytic bath can rotate sufficiently, the electrolyte can fully contact and react with the first reaction plate and the second reaction plate, the reaction efficiency is improved, the first reaction plate and the second reaction plate are provided with a plurality of through holes, the contact reaction area is increased, the reaction speed is further improved, the first electric telescopic rod machine and the second electric telescopic rod machine drive the brush plates on the telescopic rods to move up and down, the reaction pole mud of the first reaction plate and the second reaction plate is brushed down, the problem that the reaction efficiency is low due to the blockage of the reaction plates is avoided, the reaction speed is further improved, the cooling liquid in the cooling box realizes the circulation of the cooling liquid through the liquid conveying pipe under the action of the pump machine, the heat dissipation is accelerated, the heat dissipation is further accelerated by the heat dissipation fins on the outer wall of the shell of the electrolytic bath, the damage of the electrolytic bath due to overheating is avoided, and the, the utility model has the advantages of simple structure and reasonable design, not only possess efficient reaction rate, still have fabulous radiating effect, prolonged life, be fit for promoting.
Drawings
FIG. 1 is a schematic view of a cross-sectional structure of an efficient chemical electrolytic cell according to the present invention.
In the figure: the device comprises a pump 1, a cover plate 2, a liquid conveying pipe 3, a first electric telescopic rod 4, a stirring shaft 5, a first reaction plate 6, a radiating fin 7, an electrolytic bath shell 8, a cooling box 9, a motor 10, a bearing 11, a second electric telescopic rod 12, a second reaction plate 13, a telescopic rod 14, a limiting sliding groove 15, a brush plate 16 and cooling liquid 17.
Detailed Description
The technical solutions in the embodiments of the present invention will be described clearly and completely with reference to the accompanying drawings in the embodiments of the present invention, and it is obvious that the described embodiments are only some embodiments of the present invention, not all embodiments.
Referring to fig. 1, an electrolytic cell for high-efficiency chemical industry comprises an electrolytic cell shell 8 and a cooling box 9, wherein the electrolytic cell shell 8 is arranged inside the cooling box 9, the top of the electrolytic cell shell 8 is connected with a cover plate 2 through a buckle, a first reaction plate 6 and a second reaction plate 13 are symmetrically arranged on the cover plate 2, a motor 10 is arranged outside the cover plate 2, an output end of the motor 10 is provided with a stirring shaft 5, two ends of the stirring shaft 5 are symmetrically provided with bearings 11, two sides of the electrolytic cell shell 8 are symmetrically provided with a first electric telescopic rod 4 and a second electric telescopic rod 12, output ends of the first electric telescopic rod 4 and the second electric telescopic rod 12 are respectively provided with a telescopic rod 14, each telescopic rod 14 is provided with a brush plate 16, the inner side of the electrolytic cell shell 8 is symmetrically provided with a limiting sliding groove 15, the telescopic rod 14 is positioned in the limiting sliding groove 15, the outer wall of the electrolytic cell, the top end of the cooling box 9 is provided with a transfusion tube 3, the transfusion tube 3 is provided with a pump 1, and the cooling box 9 and the transfusion tube 3 are internally provided with cooling liquid 17.
The first reaction plate 6 and the second reaction plate 13 are provided with through holes uniformly distributed at equal intervals, so that the contact reaction area is increased, and the reaction rate is further improved.
The stirring shaft 5 is provided with cross rods distributed at equal intervals, the brush plate 16 is provided with hard bristles, the brush plate 16, the hard bristles and the stirring shaft 5 are of inert material structures, the stirring shaft 5 is driven to rotate through the motor 10, so that the electrolyte inside the electrolytic cell shell 8 is fully rotated and moved, the electrolyte is fully in contact reaction with the first reaction plate 6 and the second reaction plate 13, and the reaction efficiency is improved.
First electric telescopic handle machine 4 and second electric telescopic handle machine 12 drive the brush board 16 up-and-down motion on the telescopic link 14, with the reaction utmost point mud brush of first reaction plate 6 and second reaction plate 13 down, avoid leading to reaction efficiency low because of blockking up the reaction plate, further improved reaction rate.
Radiating fin 7 is the grid structure, and radiating fin 7 equidistance evenly distributed is on the outer wall of electrolysis trough shell 8, and radiating fin 7 fully submerges in coolant liquid 17, and coolant liquid 17 in the cooler bin 9 under the effect of pump machine 1, realizes the circulation of coolant liquid through transfer line 3 for the heat dissipation, and radiating fin 7 on the outer wall of electrolysis trough shell 8 has further accelerated the heat dissipation, avoids the electrolysis trough because of overheated damage, has prolonged life.
Above, only be the concrete implementation of the preferred embodiment of the present invention, but the protection scope of the present invention is not limited thereto, and any person skilled in the art is in the technical scope of the present invention, according to the technical solution of the present invention and the design of the present invention, equivalent replacement or change should be covered within the protection scope of the present invention.
Claims (4)
1. An electrolytic cell for high-efficiency chemical engineering comprises an electrolytic cell shell (8) and a cooling box (9), wherein the electrolytic cell shell (8) is arranged inside the cooling box (9), and is characterized in that the top of the electrolytic cell shell (8) is connected with a cover plate (2) through a buckle, a first reaction plate (6) and a second reaction plate (13) are symmetrically arranged on the cover plate (2), a motor (10) is arranged on the outer side of the cover plate (2), a stirring shaft (5) is arranged at the output end of the motor (10), bearings (11) are symmetrically arranged at two ends of the stirring shaft (5), a first electric telescopic rod machine (4) and a second electric telescopic rod machine (12) are symmetrically arranged at two sides of the electrolytic cell shell (8), telescopic rods (14) are arranged at the output ends of the first electric telescopic rod machine (4) and the second electric telescopic rod machine (12), and a hairbrush plate (16) is arranged on each telescopic rod (14), the inboard symmetry of electrolysis trough shell (8) is equipped with spacing spout (15), telescopic link (14) are located in spacing spout (15), the outer wall of electrolysis trough shell (8) is equipped with a plurality of radiating fin (7), the top of cooler bin (9) is equipped with transfer line (3), be equipped with pump machine (1) on transfer line (3), cooler bin (9) with the inside of transfer line (3) is equipped with coolant liquid (17).
2. An electrolyzer for high-efficiency chemical industry as claimed in claim 1, characterized in that the first reaction plate (6) and the second reaction plate (13) are provided with through holes uniformly distributed at equal intervals.
3. The electrolyzer of claim 1, characterized in that the stirring shaft (5) is provided with cross bars distributed at equal intervals, the brush plate (16) is provided with hard bristles, and the brush plate (16), the hard bristles and the stirring shaft (5) are made of inert materials.
4. The electrolytic cell for the high-efficiency chemical industry as claimed in claim 1, wherein the heat radiating fins (7) are of a grid structure, the heat radiating fins (7) are uniformly distributed on the outer wall of the electrolytic cell shell (8) at equal intervals, and the heat radiating fins (7) are fully immersed in the cooling liquid (17).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921368326.4U CN210856356U (en) | 2019-08-22 | 2019-08-22 | High-efficient electrolysis trough for chemical industry |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201921368326.4U CN210856356U (en) | 2019-08-22 | 2019-08-22 | High-efficient electrolysis trough for chemical industry |
Publications (1)
Publication Number | Publication Date |
---|---|
CN210856356U true CN210856356U (en) | 2020-06-26 |
Family
ID=71284167
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201921368326.4U Active CN210856356U (en) | 2019-08-22 | 2019-08-22 | High-efficient electrolysis trough for chemical industry |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN210856356U (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112066621A (en) * | 2020-09-02 | 2020-12-11 | 山东天润新能源材料有限公司 | Cooling device for electrolyte preparation |
-
2019
- 2019-08-22 CN CN201921368326.4U patent/CN210856356U/en active Active
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112066621A (en) * | 2020-09-02 | 2020-12-11 | 山东天润新能源材料有限公司 | Cooling device for electrolyte preparation |
CN112066621B (en) * | 2020-09-02 | 2022-06-03 | 山东天润新能源材料有限公司 | Cooling device for electrolyte preparation |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
WO2016082726A1 (en) | Electrolysis furnace | |
WO2016124034A1 (en) | Electrolytic furnace group | |
CN210856356U (en) | High-efficient electrolysis trough for chemical industry | |
CN108998806B (en) | Self-cleaning electrolytic cell | |
CN206635123U (en) | A kind of electro-chemical water handles descaler | |
CN209323015U (en) | Convenient for the electrolysis unit of heat dissipation | |
CN210410318U (en) | Stirring device for vermiculite solid culture medium | |
CN109097789A (en) | Convenient for the electrolysis unit of heat dissipation | |
CN213556893U (en) | Stirring cooling device and automatic stirring cooling equipment with same | |
CN209636327U (en) | Cyclic electrolysis device | |
CN212357415U (en) | Metal refining electrolysis unit of circulation edulcoration formula | |
CN206872968U (en) | A kind of full-automatic multi-functional oxidation aluminium system | |
CN107916439A (en) | One kind automation electrolytic cell | |
CN210367944U (en) | Non-anode-scrap electrolytic cell for silver electrolysis | |
CN213238052U (en) | Material balance buffer tank | |
CN214060663U (en) | Corner heat preservation device of aluminum electrolysis 440KA electrolytic cell | |
CN113249729A (en) | Reinforced concrete anticorrosion device for building | |
CN221166172U (en) | Reciprocating type reverse electrode electrochemical reaction device | |
CN212335319U (en) | Novel electrolytic tank limiting device | |
CN113026034A (en) | Novel electrolytic tank for hydrogen fluoride electrolysis | |
CN206666655U (en) | tungsten cathode device and electrolytic cell | |
CN220767193U (en) | Cooling device for producing hydrogen by electrolyzing water | |
CN202881413U (en) | Electrolyzing device of silver extracting machine | |
CN204939631U (en) | A kind of raw paper tinsel machine anode conducting device | |
CN210065945U (en) | Electrode foil formation stable water circulation electrolytic tank device |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
GR01 | Patent grant | ||
GR01 | Patent grant | ||
TR01 | Transfer of patent right | ||
TR01 | Transfer of patent right |
Effective date of registration: 20200814 Address after: Room 303, 35 Changqing street, Shenhe District, Shenyang City, Liaoning Province Patentee after: SHENYANG HAINAXIN TECHNOLOGY Co.,Ltd. Address before: NO.67, Wubei first village, Wuchang District, Wuhan City, Hubei Province Patentee before: Ding Liang |