CN203382830U - Combined type oxidation electrolyte tank body - Google Patents
Combined type oxidation electrolyte tank body Download PDFInfo
- Publication number
- CN203382830U CN203382830U CN201320489494.5U CN201320489494U CN203382830U CN 203382830 U CN203382830 U CN 203382830U CN 201320489494 U CN201320489494 U CN 201320489494U CN 203382830 U CN203382830 U CN 203382830U
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- cathode
- liquid storage
- cell body
- tank
- reservoir
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Abstract
The utility model discloses a combined type oxidation electrolyte tank body, which comprises a liquid storage tank, a cathode tank, a copper plate anode and a mixing system, wherein the cathode groove is movably arranged on a middle support inside a liquid storage tank body and forms an interlayer structure, together with the liquid storage tank body; the interlayer space is the liquid storage tank; the inner wall of the cathode tank is made of stainless steel while the outer is made of insulating plastic; the copper plate anode is fixed on tank wall of the upper end of the liquid storage tank; the top surface of the sidewall of the cathode tank is a little lower than the top surface of the sidewall of the liquid storage tank; an overflow hole is remained in the top surface of the sidewall of the cathode tank; electrolyte circulating cooling inlet and outlet pipeline holes are communicated with the cathode tank and the liquid storage tank respectively; the electrolyte can be circulated between the cathode tank and the liquid storage tank; an air-blowing and mixing device is arranged at the inner bottom of the cathode tank. The combined type oxidation electrolyte tank body has the characteristics of being low in floor area, small in use amount of the tank liquid, and convenient to lift, clean and wash, and guaranteeing personal safety of electricity use as a protective structure for an anode copper plate is additionally arranged on the tank body, and an anode lead is hidden in the liquid storage tank, and is particularly suitable for surface ceramic processing of a silicon-aluminum alloy piston.
Description
Technical field:
The utility model 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 oxidation trough separates with reservoir, is provided with special cooling cell body, the tank liquor circulation that makes to lower the temperature in groove and work nest reaches the cooling purpose, but floor space is large, 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.
The utility model content:
It is little that the purpose of this utility model is to provide a kind of floor space, and the tank liquor consumption is little, safe ready, the oxidation electrolyte cell body that cost is low.
The purpose of this utility model 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.
The bilayer that described liquid storage cell body is the 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, above the negative electrode cell body, is provided with suspension clamping device.
Described air blowing whipping appts is at least one plastics tubing be 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.
The accompanying drawing explanation:
The electrolyzer plan structure sketch that Fig. 1 is the utility model embodiment;
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.
in figure,5. stainless steel cathode groove, 6. double-deck PVC reservoir, 7. stirring system, 9. copper coin anode, 16. liquid storage cell walls, 17. negative electrode cell walls, 18. suspension hooks, 19. overflow ports.
Embodiment:
Below with reference to accompanying drawing, the utility model is elaborated, as shown in the figure: this novel oxidation electrolytic bath body, comprise stainless steel cathode groove 5, double-deck PVC reservoir 6, this reservoir 6 internal surface is provided with copper coin anode 9 in one week, 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, from reservoir 6, to stainless steel cathode groove 5 is interior, supplementing cooled electrolytic solution, 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 cleared 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 upward is drilled with some production wells, and the pressurized air transformed by compressed air station is stirred 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 insulating effect simultaneously.There is protective shield at copper coin anode 9 places, and fix with the plastics screw, guarantee operator's operational safety.
Claims (6)
1. a 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 the bilayer reinforcing cell body that described liquid storage cell body is the insulating sheet material welding.
3. a kind of built-up 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, above the negative electrode cell body, is provided with suspension clamping device.
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 be 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 |
---|---|---|---|
CN201320489494.5U CN203382830U (en) | 2013-08-12 | 2013-08-12 | Combined type oxidation electrolyte tank body |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CN201320489494.5U CN203382830U (en) | 2013-08-12 | 2013-08-12 | Combined type oxidation electrolyte tank body |
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CN203382830U true CN203382830U (en) | 2014-01-08 |
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CN201320489494.5U Expired - Fee Related CN203382830U (en) | 2013-08-12 | 2013-08-12 | Combined type oxidation electrolyte tank body |
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106119933A (en) * | 2016-08-21 | 2016-11-16 | 无锡瑾宸表面处理有限公司 | Security electroplating bath |
-
2013
- 2013-08-12 CN CN201320489494.5U patent/CN203382830U/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN106119933A (en) * | 2016-08-21 | 2016-11-16 | 无锡瑾宸表面处理有限公司 | Security electroplating bath |
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Legal Events
Date | Code | Title | Description |
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CF01 | Termination of patent right due to non-payment of annual fee | ||
CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140108 Termination date: 20200812 |