CN204080162U - A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool - Google Patents

A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool Download PDF

Info

Publication number
CN204080162U
CN204080162U CN201420371079.4U CN201420371079U CN204080162U CN 204080162 U CN204080162 U CN 204080162U CN 201420371079 U CN201420371079 U CN 201420371079U CN 204080162 U CN204080162 U CN 204080162U
Authority
CN
China
Prior art keywords
plating
electrolysis cathode
electroplate liquid
zinc
high purity
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.)
Withdrawn - After Issue
Application number
CN201420371079.4U
Other languages
Chinese (zh)
Inventor
沈宇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nantong Chuan Yuan Electrochemistry Science And Technology Ltd
Original Assignee
Nantong Chuan Yuan Electrochemistry Science And Technology Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Nantong Chuan Yuan Electrochemistry Science And Technology Ltd filed Critical Nantong Chuan Yuan Electrochemistry Science And Technology Ltd
Priority to CN201420371079.4U priority Critical patent/CN204080162U/en
Application granted granted Critical
Publication of CN204080162U publication Critical patent/CN204080162U/en
Withdrawn - After Issue legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Electrolytic Production Of Metals (AREA)

Abstract

The utility model relates to a kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool, and plating tank comprises plating major trough, and one by filter and the molten zinc groove that is connected of plating major trough, also comprises one and is vertically arranged on electrolysis cathode on molten zinc groove sidewall.The utility model has the advantage of: the utility model by regulate the height of telescopic bar by control to immerse zinc ball in solution number, the height of zinc ion concentration in plating solution can be controlled flexibly, ensure the stable of plating solution, and the electrolysis cathode in molten zinc groove effectively removes the foreign metal ion of electroplate liquid, plating solution pure ensured, electrolysis cathode is oval net-shaped drum and peripheral sky greatly can more effective removal noble potential impurity, centre circle can remove the metal ions such as galvanized iron, inner ring removes cupric ion, like this classification of impurities is removed, make deimpurity process more effective, the electrical current of electrolysis cathode is small area analysis, the removing of impurity can be carried out like this when not affecting plating.

Description

A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool
Technical field
The utility model relates to a kind of alkaline zinc plating electrolytic plating pool, especially a kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool.
Background technology
Electro-galvanizing is also named cold galvanizing, that workpiece is placed in electrolytic solution, that plated metal is separated out and is deposited on workpiece and forms coating, its coating is pot galvanize ratio comparatively, thinner, be generally 4-12 micron, the quality of coating is most important link, due to speed in the process of plating, distribution of current is uneven, the factor such as the dispersive ability of electroplating solution is not strong, the thickness of coating at a goods position can be caused uneven, and the corrosion resistance of coating depends primarily on thickness of coating and exposed environments, the coating that working conditions more badly needs is thicker, and the corrosion resistance of whole coating depends on that the weakest part of coating comprises the resistance to corrosion in the minimum place of local thickness, general present situation, thickness coating is added in order to obtain better solidity to corrosion, undoubtedly in the waste adding cost and zinc metal, and coating is thicker, the internal stress of coating is larger, coating easily comes off, also easily produce coarse, the flaw such as to burn, and the place that coating is excessively thin, low in glossiness, obfuscation, send out mist, easily show-through in the process of bright dipping and passivation.No matter from non-corrosibility, or outward appearance, the aspects such as machinability, all wish the homogeneity of the thickness improving product each position coating, reduce extreme difference.
The zinc-plated direct employing zine plate of conventional alkaline is as anode, and when anode quantity is very few, easy passivation is not dissolved, when anode quantity is too much, zinc concentration to be caused in solution to raise, and after anode dissolution shortens, conductivity can be affected, these all can affect the stability of plating solution, and due to the impact of time, have many foreign ions and produce, the metal ions such as such as cadmium, lead, copper, iron, time is longer, and the concentration of foreign ion is higher, and then affects quality product.Therefore just must develop one and can remove the highly purified electrolytic plating pool of foreign ion maintenance electroplate liquid in electroplate liquid, not find the same or analogous device with the utility model through retrieval.
Summary of the invention
The technical problems to be solved in the utility model is to provide one can remove the highly purified electrolytic plating pool of foreign ion maintenance electroplate liquid in electroplate liquid.
For solving the problems of the technologies described above, the technical solution of the utility model is: a kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool, comprise a plating tank, plating tank comprises plating major trough and a molten zinc groove be connected with plating major trough by filter, plating tank inwall is provided with at least one positive plate, arranges a telescopic bar directly over molten zinc groove, telescopic bar bottom arranges an insoluble hanging basket, be provided with zinc ball in hanging basket, its innovative point is: molten zinc groove sidewall arranges at least one electrolysis cathode; Described electrolysis cathode is a spirrillum reel be rolled into by rectangle mesh sheet, and rectangle net length of a film is 2000mm, and wide is 900mm;
Rectangle mesh sheet wire diameter on long side direction becomes large gradually, according to spiral of Archimedes, rectangle mesh sheet is rolled into seven layers, outer three layers is outer ring and the wire diameter of outer ring is 0.5mm ~ 0.7mm, middle two-layer for inner ring and the wire diameter of inner ring is 0.7 ~ 0.9mm, the inside two-layer centered by circle and the wire diameter of central ring is 0.9 ~ 1mm;
Rectangle mesh sheet is the outer titanizing layer of copper network, and the thickness of titanium layer is 1 ~ 3 micron.
Further, the Faradaic current of described electrolysis cathode is small area analysis, and size of current is 0.3 ~ 0.6A, and voltage is 1 ~ 1.5V.
The utility model has the advantage of: 1. the utility model effectively removes the foreign metal ion of electroplate liquid by the electrolysis cathode in molten zinc groove, the plating solution of guarantee pure.
2. electrolysis cathode of the present utility model is oval net-shaped drum and peripheral sky greatly can more effective removal noble potential impurity, centre circle can remove the metal ions such as galvanized iron, inner ring removes cupric ion, classification of impurities is removed like this, makes deimpurity process more effective.
3. the electrical current of electrolysis cathode of the present utility model is small area analysis, can carry out the removing of impurity like this when not affecting plating.
Accompanying drawing explanation
Fig. 1 is the schematic side view of the utility model alkaline zinc plating high purity electroplate liquid electrolytic plating pool.
Fig. 2 is the schematic top plan view of the utility model alkaline zinc plating high purity electroplate liquid electrolytic plating pool.
Embodiment
A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool as shown in Fig. 1 to 2, comprises a plating tank, comprises a plating tank, positive plate, direct supply and plating piece.
Have electroplating solution in plating tank, and one piece is arranged on plating tank inwall upper anode plate, also comprises peripheral hardware direct supply and a plating piece, direct supply forms loop line by wire and positive plate, plating piece, electroplating solution.
Plating tank comprises plating major trough 1, and the molten zinc groove 2 that is connected with plating major trough 1 by filter, also comprise one and be vertically arranged on electrolysis cathode 5 on molten zinc groove 2 sidewall, arrange a telescopic bar 3 directly over molten zinc groove 2, telescopic bar 3 bottom arranges an insoluble hanging basket 4, is provided with zinc ball in hanging basket 4, give insoluble hanging basket peripheral hardware flow-thru electrode equipment always simultaneously, the positive pole of direct current energized equipment is connected with hanging basket 4, and negative pole is connected with molten zinc groove 2, has electrolytic solution in molten zinc groove 2.
Described electrolysis cathode 5 is a spirrillum reel be rolled into by rectangle mesh sheet as shown in Figure 1, and rectangle net length of a film is 2000mm, and wide is 900mm; Rectangle mesh sheet wire diameter on long side direction becomes large gradually, according to spiral of Archimedes, rectangle mesh sheet is rolled into seven layers, outer three layers is outer ring and the wire diameter of outer ring is 0.5mm ~ 0.7mm, middle two-layer for inner ring and the wire diameter of inner ring is 0.7 ~ 0.9mm, the inside two-layer centered by circle and the wire diameter of central ring is 0.9 ~ 1mm; The wire diameter of central ring is 1mm; Rectangle mesh sheet is the outer titanizing layer of copper network, and the thickness of titanium layer is 1 ~ 3 micron.
The Faradaic current of electrolysis cathode 5 is small area analysis, and size of current is 0.3 ~ 0.6A, and voltage is 1 ~ 1.5V.
Its principle of work is: the utility model device adds electrolysis cathode in molten zinc groove, electrolysis cathode is the elliptical shaped cylinders of certain specification, and outer field aperture is greater than the aperture of internal layer by small area analysis electrolysis, different impurity metal ions is carried out layered shaping, remove the metal ion such as copper, lead, iron, chromium in electroplate liquid successively, ensure that the pure of plating solution.

Claims (2)

1. an alkaline zinc plating high purity electroplate liquid electrolytic plating pool, comprise a plating tank, plating tank comprises plating major trough and a molten zinc groove be connected with plating major trough by filter, plating tank inwall is provided with at least one positive plate, directly over molten zinc groove, a telescopic bar is set, telescopic bar bottom arranges an insoluble hanging basket, is provided with zinc ball, it is characterized in that in hanging basket: molten zinc groove sidewall arranges at least one electrolysis cathode; Described electrolysis cathode is a spirrillum reel be rolled into by rectangle mesh sheet, and rectangle net length of a film is 2000mm, and wide is 900mm;
Rectangle mesh sheet wire diameter on long side direction becomes large gradually, according to spiral of Archimedes, rectangle mesh sheet is rolled into seven layers, outer three layers is outer ring and the wire diameter of outer ring is 0.5mm ~ 0.7mm, middle two-layer for inner ring and the wire diameter of inner ring is 0.7 ~ 0.9mm, the inside two-layer centered by circle and the wire diameter of central ring is 0.9 ~ 1mm;
Rectangle mesh sheet is the outer titanizing layer of copper network, and the thickness of titanium layer is 1 ~ 3 micron.
2. a kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool according to claim 1, is characterized in that: the Faradaic current of described electrolysis cathode is small area analysis, and size of current is 0.3 ~ 0.6A, and voltage is 1 ~ 1.5V.
CN201420371079.4U 2014-07-07 2014-07-07 A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool Withdrawn - After Issue CN204080162U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420371079.4U CN204080162U (en) 2014-07-07 2014-07-07 A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420371079.4U CN204080162U (en) 2014-07-07 2014-07-07 A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool

Publications (1)

Publication Number Publication Date
CN204080162U true CN204080162U (en) 2015-01-07

Family

ID=52172898

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420371079.4U Withdrawn - After Issue CN204080162U (en) 2014-07-07 2014-07-07 A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool

Country Status (1)

Country Link
CN (1) CN204080162U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104060318A (en) * 2014-07-07 2014-09-24 南通创源电化学科技有限公司 Electroplating tank for alkaline zinc-plated electroplating liquid high in purity
WO2017084056A1 (en) * 2015-11-19 2017-05-26 蔡慧勤 Zinc plating device for forming zinc ring on metal fitting

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104060318A (en) * 2014-07-07 2014-09-24 南通创源电化学科技有限公司 Electroplating tank for alkaline zinc-plated electroplating liquid high in purity
WO2017084056A1 (en) * 2015-11-19 2017-05-26 蔡慧勤 Zinc plating device for forming zinc ring on metal fitting

Similar Documents

Publication Publication Date Title
CN2787685Y (en) Reticular anode arrangement of electroplating tank
CN104060318B (en) A kind of alkaline zinc plating high-purity electroplate liquid electroplating pool
CN101397691B (en) Apparatus and technology for controlling and improving plating solution PH value on fingerprint resistant production chain
CN204080162U (en) A kind of alkaline zinc plating high purity electroplate liquid electrolytic plating pool
CN205688030U (en) A kind of copper refining electrolysis bath circulating remove impurity formula
CN204080160U (en) A kind of alkaline zinc plating electrolytic plating pool
CN102108531B (en) Impurity removing method for nickel electroplating solution and impurity removing equipment thereof
CN102534733A (en) Electroplating device and electroplating method
CN107937970A (en) New VCP lines copper-plated anode bag
CN204174298U (en) A kind of supplementary anode for Acidic zinc-nickel alloy plating
CN104099658A (en) Auxiliary anode for use in acid zinc-nickel alloy electroplating
CN101397690A (en) Double cathode electrolytic tank on roll bending galvanizing continuous automatic production line
CN103358614A (en) Steel sheet with stanniferous coating and preparation method thereof
CN104204307B (en) Operate the anode and method of electrolysis cells
CN207537590U (en) Electroplanting device
CN104512946A (en) Online electrodeposition method of metal wastewater, and apparatus thereof
US4006072A (en) Device for eliminating impure ions in chromium plating bath
CN203486944U (en) Online electro-deposition device for metal waste water
CN210215606U (en) Electroplating device
CN208362510U (en) A kind of hardware stamping electroplating surface device
CN203728947U (en) PCB (Printed Circuit Board) electroplating copper urn
US2288762A (en) Zinc coated ferrous article
CN106676618A (en) Improved gun-color electroplating meshed anode
CN210194007U (en) Wet electrolytic refining device capable of changing electrolyte circulation mode
CN105648485A (en) Cyanide-free silver electroplating liquid

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
AV01 Patent right actively abandoned

Granted publication date: 20150107

Effective date of abandoning: 20160511

C25 Abandonment of patent right or utility model to avoid double patenting