CN221275915U - Anodic oxidation electrolytic tank - Google Patents
Anodic oxidation electrolytic tank Download PDFInfo
- Publication number
- CN221275915U CN221275915U CN202323240839.6U CN202323240839U CN221275915U CN 221275915 U CN221275915 U CN 221275915U CN 202323240839 U CN202323240839 U CN 202323240839U CN 221275915 U CN221275915 U CN 221275915U
- Authority
- CN
- China
- Prior art keywords
- electrolytic tank
- anodic oxidation
- bottom plate
- electrolysis trough
- fixedly arranged
- 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.)
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- 230000003647 oxidation Effects 0.000 title claims abstract description 17
- 238000007254 oxidation reaction Methods 0.000 title claims abstract description 17
- 239000003792 electrolyte Substances 0.000 claims abstract description 24
- 229910001200 Ferrotitanium Inorganic materials 0.000 claims abstract description 4
- 229910045601 alloy Inorganic materials 0.000 claims abstract description 4
- 239000000956 alloy Substances 0.000 claims abstract description 4
- 238000005868 electrolysis reaction Methods 0.000 claims description 23
- 229910052751 metal Inorganic materials 0.000 claims description 17
- 239000002184 metal Substances 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 15
- 210000005056 cell body Anatomy 0.000 claims description 10
- 230000003014 reinforcing effect Effects 0.000 claims description 8
- WABPQHHGFIMREM-UHFFFAOYSA-N lead(0) Chemical compound [Pb] WABPQHHGFIMREM-UHFFFAOYSA-N 0.000 claims description 5
- 239000002699 waste material Substances 0.000 claims description 5
- 229910000831 Steel Inorganic materials 0.000 claims description 3
- 229910001256 stainless steel alloy Inorganic materials 0.000 claims description 3
- 239000010959 steel Substances 0.000 claims description 3
- 239000000463 material Substances 0.000 claims description 2
- 210000004027 cell Anatomy 0.000 description 9
- 230000000694 effects Effects 0.000 description 4
- 230000005611 electricity Effects 0.000 description 4
- 230000003068 static effect Effects 0.000 description 4
- 230000006378 damage Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 208000027418 Wounds and injury Diseases 0.000 description 2
- 230000000903 blocking effect Effects 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 208000014674 injury Diseases 0.000 description 2
- 238000013021 overheating Methods 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000005684 electric field Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000126 substance Substances 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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
Landscapes
- Electrolytic Production Of Metals (AREA)
Abstract
The utility model relates to the technical field of anodic oxidation equipment and discloses an anodic oxidation electrolytic tank, which comprises an electrolytic tank bottom plate, wherein the top end of the electrolytic tank bottom plate is fixedly provided with an electrolytic tank body, the electrolytic tank body is made of titanium steel alloy, the top end of the electrolytic tank bottom plate is fixedly provided with a sliding plate, two electric sliders are slidably arranged on the sliding plate, electrolyte sensors are arranged in the electrolytic tank body, the bottom ends of the electric sliders are fixedly provided with insulating mounting plates, and the bottom ends of the insulating mounting plates are fixedly provided with power-on electrodes.
Description
Technical Field
The utility model relates to the technical field of anodic oxidation equipment, in particular to an anodic oxidation electrolytic tank.
Background
The anodic oxidation technology needs to use an electrolytic tank for chemical electrolysis, most of the electrodes of the existing electrolytic tank are fixed with the electrolytic tank, the reinstalled electrodes are required to be frequently disassembled according to different electrolyte characteristics, the electrode pole distance can not be automatically adjusted according to the electrolyte, and the universality is poor.
Disclosure of utility model
In order to overcome the defects in the prior art, the utility model provides an anodic oxidation electrolytic cell, which solves the problems that most of electrodes of the existing electrolytic cell in the prior art are fixed with the electrolytic cell, the reinstalled electrodes are required to be frequently disassembled according to different electrolyte characteristics, the electrode pole distance cannot be automatically adjusted according to the electrolyte, and the universality is poor.
The utility model provides the following technical scheme: the utility model provides an anodic oxidation electrolysis trough, includes the electrolysis trough bottom plate, the top fixed mounting of electrolysis trough bottom plate has the electrolysis trough cell body, the material of electrolysis trough cell body is titanium steel alloy, the top fixed mounting of electrolysis trough bottom plate has the sliding plate, slidable mounting has two electronic sliders on the sliding plate, the inside of electrolysis trough cell body is provided with electrolyte sensor, the bottom of electronic slider is all fixed mounting has insulating mounting panel, the bottom of insulating mounting panel is all fixed mounting has the electrified electrode, all be provided with the circular telegram interface on the electrified electrode. When the electrolyte sensor is used, after the electrolyte sensor is contacted with a solution to be electrolyzed, certain characteristics of the electrolyte, such as conductivity, concentration and the like, are automatically analyzed, then the data are transmitted to an external control computer, at the moment, a user can adjust the distance between two electrified electrodes through the data, an electric sliding block drives an insulating mounting plate and the electrified electrodes to slide on a sliding plate so as to change the polar distance between the two electrified electrodes, when the polar distance is changed, the electrolysis effect is also changed, and the problems that most of the electrodes of the existing electrolytic tank are fixed with the electrolytic tank in actual use, the reloaded electrodes are required to be frequently detached according to the different characteristics of the electrolyte, and the polar distance of the electrodes cannot be automatically adjusted according to the electrolyte, so that the universality is poor are effectively solved.
Further, the joint of the sliding plate and the bottom plate of the electrolytic tank is fixedly provided with a reinforcing rib, and the reinforcing rib and the sliding plate are made of stainless steel alloy. When the electric sliding block is used, the reinforcing ribs can further enhance the connection between the sliding plate and the bottom plate of the electrolytic tank, so that the structural stability of the sliding plate is enhanced, the structural strength is increased, and the sliding plate is prevented from being damaged after the electric sliding block frequently slides.
Further, a liquid discharge pump is fixedly arranged in front of the electrolytic tank body, and a waste liquid filter is connected to the liquid discharge pump. When the electrolyte is used, after the internal electrolysis of the electrolyte is finished, the waste liquid is required to be treated, at the moment, the liquid discharge pump can be turned on, and the waste liquid is led into the filter for filtration and then discharged.
Furthermore, two splash-proof plates are fixedly arranged at the top end of the electrolytic tank body, and the side projection shapes of the splash-proof plates are triangular. When the electrolytic bath is used, in order to prevent personnel injury caused by splashing of the electrolyte in the electrolytic process, two splash-proof plates can be arranged at the top end of the electrolytic bath body, and the splash-proof plates are in a shed shape and have a good liquid blocking effect.
Furthermore, a layer of lead metal is fixedly arranged in the electrolytic tank body to serve as an inner liner. When the lead metal lining is used, electrons can frequently move in the electrolysis process, so that the inner wall of the electrolytic tank body can be worn, and lead metal with good wear resistance can be used as the lining to prevent excessive wear.
Furthermore, a plurality of grounding metal rods are fixedly arranged at the bottom end of the bottom plate of the electrolytic tank, the grounding metal rods are made of steel metal, and the grounding metal rods extend into the ground. When the electrolytic tank is used, the electrolytic tank body is made of metal, so that more static electricity can occur during electrolysis, and the grounded metal rod can be inserted into the ground at the moment, so that the bottom end of the bottom plate of the electrolytic tank is stabilized, and the static electricity on the outer wall of the electrolytic tank body can be led into the ground.
The utility model has the technical effects and advantages that:
1. According to the utility model, the problems that most of the electrodes of the existing electrolytic tank are fixed with the electrolytic tank, the reinstalled electrodes are required to be frequently disassembled according to different electrolyte characteristics, the electrode pole distance cannot be automatically adjusted according to the electrolyte, and the universality is poor can be effectively solved in actual use by arranging the electrolytic tank bottom plate, the electrolytic tank body, the sliding plate, the electric sliding block, the insulating mounting plate and the electrified electrode.
2. When the anti-splashing device is used, two anti-splashing plates can be arranged at the top end of the electrolytic tank body in order to prevent personnel injury caused by splashing of electrolyte in the electrolytic process, and the anti-splashing plates are in a shed shape and have a good liquid blocking effect.
Drawings
Fig. 1 is a schematic perspective view of a first structure of the present utility model.
Fig. 2 is a schematic perspective view of a second structure of the present utility model.
Fig. 3 is a schematic perspective view of a third structure of the present utility model.
Fig. 4 is a schematic elevational view of the structure of the present utility model.
The reference numerals are: 100. a bottom plate of the electrolytic cell; 110. an electrolytic tank body; 111. a sliding plate; 112. an electric slide block; 113. an insulating mounting plate; 114. energizing the electrode; 115. an anti-splash plate; 116. a liquid discharge pump; 117. reinforcing ribs; 118. a grounded metal rod.
Detailed Description
The embodiments of the present utility model will be clearly and completely described below with reference to the drawings in the present utility model, and the configurations of the structures described in the following embodiments are merely examples, and the anodic oxidation electrolytic cell according to the present utility model is not limited to the structures described in the following embodiments, and all other embodiments obtained by a person having ordinary skill in the art without making any creative effort are within the scope of the present utility model.
Embodiment one:
Referring to fig. 1 and 2, the utility model provides an anodic oxidation electrolytic cell, which comprises an electrolytic cell bottom plate 100, wherein an electrolytic cell body 110 is fixedly arranged at the top end of the electrolytic cell bottom plate 100, the electrolytic cell body 110 is made of titanium steel alloy, a sliding plate 111 is fixedly arranged at the top end of the electrolytic cell bottom plate 100, two electric sliding blocks 112 are slidably arranged on the sliding plate 111, an electrolyte sensor is arranged in the electrolytic cell body 110, insulating mounting plates 113 are fixedly arranged at the bottom ends of the electric sliding blocks 112, energizing electrodes 114 are fixedly arranged at the bottom ends of the insulating mounting plates 113, and energizing interfaces are arranged on the energizing electrodes 114.
Reinforcing ribs 117 are fixedly arranged at the connecting positions of the sliding plate 111 and the electrolytic tank bottom plate 100, and the reinforcing ribs 117 and the sliding plate 111 are made of stainless steel alloy.
A liquid discharge pump 116 is fixedly arranged in front of the electrolytic tank body 110, and a waste liquid filter is connected to the liquid discharge pump 116.
Working principle: the change of the distance between the energizing electrodes 114 affects the electric field distribution in the electrolyte, and thus affects the electrolytic reaction, specifically, the energizing electrodes 114 are too close, which can increase the current density and improve the electrolytic efficiency, but also easily cause short circuit between the energizing electrodes 114 and overheating of the electrolyte, and may even damage the structure of the electrolytic tank body 110; in contrast, the distance between the power-on electrodes 114 is too far, although the problem of short-circuit and overheating can be prevented, the current density is reduced, and the electrolysis efficiency is lowered, so that the user can manually change the distance between the power-on electrodes 114 according to the characteristics of the electrolyte to obtain a better electrolysis effect, firstly, after the electrolyte sensor is contacted with the solution to be electrolyzed, some characteristics of the electrolyte, such as conductivity, concentration and the like, are automatically analyzed, and then the data are transmitted to an external control computer, at this time, the user can adjust the distance between the two power-on electrodes 114 through the data, and the electric sliding block 112 drives the insulating mounting plate 113 and the power-on electrodes 114 to slide on the sliding plate 111 to change the polar distance between the two power-on electrodes 114, and when the polar distance is changed, the electrolysis effect is also changed.
Embodiment two:
Referring to fig. 1, the second embodiment differs from the first embodiment in that: two splash-proof plates 115 are fixedly arranged at the top end of the electrolytic tank body 110, and the side projection shapes of the splash-proof plates 115 are triangular.
A layer of lead metal is fixedly installed inside the electrolytic cell body 110 as an inner liner.
The bottom end of the bottom plate 100 of the electrolytic tank is fixedly provided with a plurality of grounding metal rods 118, the grounding metal rods 118 are made of steel metal, and the grounding metal rods 118 extend into the ground.
Working principle: when in use, because the electrolytic tank body 110 is made of metal, more static electricity can be generated during electrolysis, and the grounding metal rod 118 can be inserted into the ground at the moment, so that the bottom end of the electrolytic tank bottom plate 100 can be stabilized, and static electricity on the outer wall of the electrolytic tank body 110 can be led into the ground.
The last points to be described are: in the description of the present application, unless otherwise specified and defined, the terms "mounted," "connected," and "connected" are to be construed broadly and may be mechanical or electrical, may be in communication with each other between two elements, may be in direct communication, and may be used merely to indicate relative positional relationships, which may be altered when the absolute position of the object being described is changed.
Claims (6)
1. The utility model provides an anodic oxidation electrolysis trough, includes electrolysis trough bottom plate (100), its characterized in that, the top fixed mounting of electrolysis trough bottom plate (100) has electrolysis trough cell body (110), the material of electrolysis trough cell body (110) is titanium steel alloy, the top fixed mounting of electrolysis trough bottom plate (100) has sliding plate (111), slidable mounting has two electronic slider (112) on sliding plate (111), the inside of electrolysis trough cell body (110) is provided with electrolyte sensor, the bottom of electronic slider (112) all fixed mounting has insulating mounting panel (113), the bottom of insulating mounting panel (113) all fixed mounting has circular telegram electrode (114), all be provided with the circular telegram interface on circular telegram electrode (114).
2. An anodic oxidation electrolyzer as claimed in claim 1, characterized in that: reinforcing ribs (117) are fixedly arranged at the connecting positions of the sliding plates (111) and the bottom plate (100) of the electrolytic tank, and the reinforcing ribs (117) and the sliding plates (111) are made of stainless steel alloy.
3. An anodic oxidation electrolyzer as claimed in claim 1, characterized in that: a liquid discharge pump (116) is fixedly arranged in front of the electrolytic tank body (110), and a waste liquid filter is connected to the liquid discharge pump (116).
4. An anodic oxidation electrolyzer as claimed in claim 1, characterized in that: two splash-proof plates (115) are fixedly arranged at the top end of the electrolytic tank body (110), and the side projection shapes of the splash-proof plates (115) are triangular.
5. An anodic oxidation electrolyzer as claimed in claim 1, characterized in that: and a layer of lead metal is fixedly arranged in the electrolytic tank body (110) to serve as an inner liner.
6. An anodic oxidation electrolyzer as claimed in claim 1, characterized in that: the bottom end of the electrolytic tank bottom plate (100) is fixedly provided with a plurality of grounding metal rods (118), the grounding metal rods (118) are made of steel metal, and the grounding metal rods (118) extend into the ground.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323240839.6U CN221275915U (en) | 2023-11-29 | 2023-11-29 | Anodic oxidation electrolytic tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202323240839.6U CN221275915U (en) | 2023-11-29 | 2023-11-29 | Anodic oxidation electrolytic tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN221275915U true CN221275915U (en) | 2024-07-05 |
Family
ID=91709613
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202323240839.6U Active CN221275915U (en) | 2023-11-29 | 2023-11-29 | Anodic oxidation electrolytic tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN221275915U (en) |
-
2023
- 2023-11-29 CN CN202323240839.6U patent/CN221275915U/en active Active
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