CN103397362A - Combined-type oxidation electrolyte tank - Google Patents
Combined-type oxidation electrolyte tank Download PDFInfo
- Publication number
- CN103397362A CN103397362A CN2013103483127A CN201310348312A CN103397362A CN 103397362 A CN103397362 A CN 103397362A CN 2013103483127 A CN2013103483127 A CN 2013103483127A CN 201310348312 A CN201310348312 A CN 201310348312A CN 103397362 A CN103397362 A CN 103397362A
- Authority
- CN
- China
- Prior art keywords
- tank
- cathode
- liquid storage
- cell body
- type oxidation
- 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.)
- Pending
Links
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
The invention discloses a combined-type oxidation electrolyte tank. The combined-type oxidation electrolyte tank comprises a liquid storage tank, a cathode tank, a copper plate anode and a stirring system, wherein the cathode tank is movably placed on a middle support in the liquid storage tank to form an interlayer structure with the liquid storage tank, and the interlayer space is the liquid storage tank; the inner wall of the cathode tank is made from stainless steel, the outer wall of the cathode tank is made from insulating plastic, and the copper plate anode is fixed on the tank wall at the upper end of the liquid storage tank; the top surface of the sidewall of the cathode tank is slightly lower than the top surface of the sidewall of the liquid storage tank, and an overflow port is reserved in the top surface of the sidewall of the cathode tank; an electrolyte circulation cooling inlet-outlet pipeline port is communicated with the cathode tank and the liquid storage tank respectively, and an electrolyte can be circulated between the cathode tank and the liquid storage tank; a gas-blowing stirring device is arranged at the inner bottom of the cathode tank. The combined-type oxidation electrolyte tank has the characteristics of small floor area and low tank liquor dosage, and is convenient to lift to clear and clean; a protection structure for the anode copper plate is added on the tank, and an anode conductive wire is hidden in the liquid storage groove, thus ensuring power utilization safety and personal safety. The combined-type oxidation electrolyte tank is especially suitable for a vitrification treatment on a silicon-aluminium alloy piston surface.
Description
A kind of technical field:
The present invention relates to field of metal surface treatment technology, particularly a kind of novel combination type oxidation electrolyte cell body.
Background technology:
Differential arc oxidation electrolytic solution cell body is generally taked Split type device, and namely oxidation trough separates with reservoir, is provided with special cooling cell body, make the tank liquor circulation in cooling groove and work nest reach the cooling purpose, but floor space is large, and the tank liquor consumption is large, is unfavorable for the management of production plant.Differential arc oxidation process Anodic wire leaks outside, and has potential safety hazard.
Summary of the invention:
The purpose of this invention is to provide a kind of floor space little, the tank liquor consumption is little, safe ready, the oxidation electrolyte cell body that cost is low.
purpose of the present invention realizes by following technical proposals: a kind of built-up type oxidation electrolyte cell body, comprise reservoir, cathode can, copper coin anode and stirring system, the middle part that described cathode can activity is placed in described liquid storage cell body is supported, form sandwich structure with the reservoir body, mezzanine space is reservoir, the inwall of cathode can is stainless steel, outer wall is insulating plastics, the copper coin anode is fixed on the cell wall of reservoir upper end, the sidewall end face of described cathode can is a little less than reservoir sidewall end face, the sidewall end face of cathode can leaves overflow port, the cooling inlet/outlet pipe of circulation of elecrolyte road junction is communicated with respectively cathode can and reservoir, electrolytic solution can circulate between cathode can and reservoir, described cathode can inner bottom part is provided with the air blowing whipping appts.
Described liquid storage cell body is that the bilayer of insulating sheet material welding is reinforced cell body.
Described copper coin anode ring week is fixed on liquid storage cell body inside top wall, and pair structure of copper coin anodic protection is arranged.
Described cathode can overflow port structure is: top end face one end of negative electrode cell wall is lower, and the gauging line of its height during with the workpiece surface ceramic treatment maintains an equal level.
The two side of described negative electrode cell body symmetry is provided with suspension hook, is provided with suspension clamping device above the negative electrode cell body.
Described air blowing whipping appts is at least one plastics tubing that is fixed at the bottom of cathode can, and plastics tubing is provided with some ventilating pits, and plastics tubing outer end interface connects the compressed air-feed pipeline.
The characteristics of this cell body are:
1, floor space is little, and the tank liquor consumption is few;
2, the cell body inner chamber separates with housing, the cleaning of being convenient to sling, cleaning;
3, increase the safeguard structure of antianode copper coin on cell body, positive wire is hidden in reservoir, has guaranteed the electricity consumption personnel safety.
Description of drawings:
Fig. 1 is the electrolyzer plan structure sketch of the embodiment of the present invention;
Fig. 2 is the A-A diagrammatic cross-sectional view in Fig. 1;
Fig. 3 is the B-B diagrammatic cross-sectional view in Fig. 1.
Embodiment:
The present invention is described in detail below with reference to accompanying drawing, as shown in the figure: this novel oxidation electrolytic bath body, comprise stainless steel cathode groove 5, double-deck PVC reservoir 6, these 6 one weeks of internal surface of reservoir are provided with copper coin anode 9, wherein stainless steel cathode groove 5 and reservoir 6 are combined, and can separate, stainless steel cathode groove 5 two ends are provided with suspension hook 18, be convenient to utilize row to hang 10 sling cleaning, cleanings, greatly reduced floor space, save electrolytic solution, made the production plant layout more neat, be convenient to the production and administration that standardizes.Negative electrode cell wall 17 is made for stainless material, the double negative electrode of doing; Stainless steel cathode groove 5 one ends are lower, be provided with overflow port 19, the gauging line of its height during with the workpiece surface ceramic treatment maintains an equal level, while by water pump, supplementing cooled electrolytic solution to stainless steel cathode groove 5 is interior from reservoir 6, electrolytic solution automatically overflows and flows in reservoir from overflow port 19 after exceeding gauging line, guarantees the circulation of elecrolyte utilization.Stainless steel cathode groove 5 two ends are provided with suspension hook 18, are convenient to hang 10 with row and sling and clear up.Stirring system 7 is made and is formed by the PPR pipe, is fixed on stainless steel cathode groove 5 bottoms, and an end up is drilled with some production wells, and the pressurized air that transforms by compressed air station stirs the electrolytic solution in stainless steel cathode groove 5, improves electrolytical homogeneity in solution.Copper coin anode 9 materials are copper coin, are fixed on above reservoir 6, and, around a circle, are convenient to be connected with workpiece.
As further improvement in the technical proposal, described liquid storage cell wall 16 is welded by the PP plate, and the support of reinforcing is arranged, and prevents cell body distortion spalling, plays simultaneously insulating effect.There is protective shield at copper coin anode 9 places, and with the plastics screw, fix, and guarantee operator's operational safety.
Claims (6)
1. built-up type oxidation electrolyte cell body, comprise reservoir, cathode can, copper coin anode and stirring system, it is characterized in that: the middle part that described cathode can activity is placed in described liquid storage cell body is supported, form sandwich structure with the reservoir body, mezzanine space is reservoir, the inwall of cathode can is stainless steel, outer wall is insulating plastics, the copper coin anode is fixed on the cell wall of reservoir upper end, the sidewall end face of described cathode can is a little less than reservoir sidewall end face, the sidewall end face of cathode can leaves overflow port, the cooling inlet/outlet pipe of circulation of elecrolyte road junction is communicated with respectively cathode can and reservoir, electrolytic solution can circulate between cathode can and reservoir, described cathode can inner bottom part is provided with the air blowing whipping appts.
2. a kind of built-up type oxidation electrolyte cell body according to claim 1, is characterized in that described liquid storage cell body is the bilayer reinforcing cell body of insulating sheet material welding.
3. a kind of novel combination type oxidation electrolyte cell body according to claim 1 and 2, is characterized in that being fixed on liquid storage cell body inside top wall in described copper coin anode ring week, and pair structure of copper coin anodic protection arranged.
4. a kind of built-up type oxidation electrolyte cell body according to claim 1, it is characterized in that described cathode can overflow port structure is: top end face one end of negative electrode cell wall is lower, and the gauging line of its height during with the workpiece surface ceramic treatment maintains an equal level.
5. a kind of built-up type oxidation electrolyte cell body according to claim 1, is characterized in that the two side of described negative electrode cell body symmetry is provided with suspension hook, is provided with suspension clamping device above the negative electrode cell body.
6. a kind of built-up type oxidation electrolyte cell body according to claim 1, it is characterized in that described air blowing whipping appts is at least one plastics tubing that is fixed at the bottom of cathode can, plastics tubing is provided with some ventilating pits, and plastics tubing outer end interface connects the compressed air-feed pipeline.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013103483127A CN103397362A (en) | 2013-08-12 | 2013-08-12 | Combined-type oxidation electrolyte tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2013103483127A CN103397362A (en) | 2013-08-12 | 2013-08-12 | Combined-type oxidation electrolyte tank |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN103397362A true CN103397362A (en) | 2013-11-20 |
Family
ID=49561057
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN2013103483127A Pending CN103397362A (en) | 2013-08-12 | 2013-08-12 | Combined-type oxidation electrolyte tank |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103397362A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT15942U1 (en) * | 2017-04-25 | 2018-10-15 | Edlmair Kunststofftechnik Gmbh | DOUBLE-WALLED STORAGE TANK FOR STATIONARY REDOX FLOW BATTERIES |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1785912A (en) * | 2004-12-07 | 2006-06-14 | 上海施迈尔精密陶瓷有限公司 | Light metal surface micro plasma ceramic coating technology |
| CN101550579A (en) * | 2009-04-16 | 2009-10-07 | 哈尔滨工业大学 | Method and device for processing restrained micro-space micro-arc oxidation of electric field on the surface of large-size workpiece |
| CN101660186A (en) * | 2009-10-09 | 2010-03-03 | 哈尔滨工业大学 | Low-noise micro-arc oxidation device |
-
2013
- 2013-08-12 CN CN2013103483127A patent/CN103397362A/en active Pending
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1785912A (en) * | 2004-12-07 | 2006-06-14 | 上海施迈尔精密陶瓷有限公司 | Light metal surface micro plasma ceramic coating technology |
| CN101550579A (en) * | 2009-04-16 | 2009-10-07 | 哈尔滨工业大学 | Method and device for processing restrained micro-space micro-arc oxidation of electric field on the surface of large-size workpiece |
| CN101660186A (en) * | 2009-10-09 | 2010-03-03 | 哈尔滨工业大学 | Low-noise micro-arc oxidation device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| AT15942U1 (en) * | 2017-04-25 | 2018-10-15 | Edlmair Kunststofftechnik Gmbh | DOUBLE-WALLED STORAGE TANK FOR STATIONARY REDOX FLOW BATTERIES |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102839407A (en) | Piston rapid aluminum oxidation single machine | |
| CN210826392U (en) | Electrolytic device for industrial production of 5N high-purity copper | |
| CN203382830U (en) | Combined type oxidation electrolyte tank body | |
| CN205382221U (en) | Metalwork anodic oxidation treatment device | |
| CN103397362A (en) | Combined-type oxidation electrolyte tank | |
| CN201990120U (en) | Low-temperature liquid storage tank | |
| CN104294313A (en) | Electrochemical gold dissolving device and method | |
| CN101792911B (en) | Sodium hypochlorite generator electrolyzer | |
| CN203878226U (en) | Electrolytic tank structure | |
| CN202755081U (en) | Piston fast aluminum oxidation single machine | |
| CN100351640C (en) | Loading device | |
| CN103397364A (en) | Aluminum-silicon alloy surface ceramic treatment method and apparatus | |
| CN213113556U (en) | Anodic oxidation tank capable of realizing uniform distribution of electrolyte | |
| CN202272918U (en) | Cooling water tank for steel wire production technology | |
| KR101889498B1 (en) | Elevating hydrogen water production equipment | |
| CN206768256U (en) | A kind of nickel plating apparatus | |
| CN205635825U (en) | Aluminum alloy welded joint's micro -arc oxidation corrosion resistant protector | |
| CN201545915U (en) | Gas-liquid gravity-flow circulating type hydrogen electrolyzer | |
| CN203429271U (en) | Ceramic treatment device for surface of aluminum-silicon alloy | |
| CN202181355U (en) | Oxyhydrogen generating device | |
| CN103361673A (en) | Titanium cylinder electrolysis machine | |
| CN210104083U (en) | Alkaline etching liquid copper recovery and regeneration device | |
| CN206666655U (en) | tungsten cathode device and electrolytic cell | |
| CN201777923U (en) | Water tank capable of controlling water level and water temperature for treating landfill leachate | |
| CN206570414U (en) | A kind of electro-deposition of metal insoluble anode |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |
Application publication date: 20131120 |