CN203128675U - Cathode plate for electrolytic copper powder - Google Patents
Cathode plate for electrolytic copper powder Download PDFInfo
- Publication number
- CN203128675U CN203128675U CN 201220726675 CN201220726675U CN203128675U CN 203128675 U CN203128675 U CN 203128675U CN 201220726675 CN201220726675 CN 201220726675 CN 201220726675 U CN201220726675 U CN 201220726675U CN 203128675 U CN203128675 U CN 203128675U
- Authority
- CN
- China
- Prior art keywords
- cathode plate
- hangers
- negative plate
- copper powder
- electrolytic copper
- 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.)
- Expired - Lifetime
Links
Images
Abstract
The utility model discloses a cathode plate for the electrolytic copper powder, belonging to the technical field of the electrolytic copper powder. The cathode plate consists of a copper cathode plate main body, a conductive hanging lug and an insulation hanging lug, wherein the conductive hanging lug and the insulation hanging lug are respectively arranged on two sides of the top of the cathode plate and in bilateral symmetry; and the conductive hanging lug is divided into an insulation layer part and a conductive part. The cathode plate can avoid the defects that an existing cathode plate is easy to corrode and copper dense deposits are easy to produce in local part, and has the characteristics of simplicity in production and low cost, the service life of the cathode plate can be prolonged and the reject ratio of a product can be reduced.
Description
Technical field
The utility model belongs to the electrolytic copper powder technical field, is specifically related to a kind of electrolytic copper powder negative plate.
Background technology
The negative plate that uses in the production of current electrolysis copper powder is mainly made by copper coin, is connected with busbar by copper extension bar or copper hangers.In electrolyzer, negative plate main body top has sub-fraction to be exposed to the top of electrolysis liquid surface usually.In electrolytic process, because the ununiformity of electric current, on liquid level place battery lead plate, can generate the fine and close thing band of a flat copper gradually, this fine and close thing is difficult to be eliminated, and not the product that needs, reduced the product percent of pass of whole production line, also had influence on the negative plate liquid level and operate with the powder of scraping of lower section; Simultaneously because electrolytic solution is acid system, and have higher temperature, partly can be corroded gradually under the effect at oxygen being exposed to airborne battery lead plate near the liquid level, until fracture, its reaction formula is:
Cu+H
2SO
4+1/2O
2=CuSO
4+H
2O
This reaction will be shortened the work-ing life of negative plate.
At present, for two problems that run in the use of above-mentioned electrolytic copper powder negative plate, method commonly used is that near the negative plate liquid level applies a circle corrosion-resisting resin, or sprays a circle plastic coating; But because the corrosive nature of acid mist does not have the part of coating still can progressively be corroded, and then has influence on the bond state of following coating on negative plate top, cause coating shedding; This coating coverage is big in addition, has increased cost of manufacture, whole negative plate need be handled when adopting thermospray, and operation easier is big.
The utility model content
The purpose of this utility model is to provide a kind of electrolytic copper powder negative plate.
A kind of electrolytic copper powder negative plate is made up of copper cathode sheets main body 1, conduction hangers 2 and insulation hangers 5, and described conduction hangers 2 and insulation hangers 5 are positioned at the both sides at negative plate top, are left-right symmetry; Its conduction hangers 2 is divided into edge layer segment 3 and current-carrying part 4 because being coated with insulating layer coating.
Hangers is by being connected with the material rivet or welding with the mode of connection of negative plate main body.
The beneficial effects of the utility model are: the negative plate main body is immersed under the electrolysis liquid surface, has eliminated corrosion on the negative plate face and the generation of fine and close thing, can improve the accepted product percentage of product, prolongs negative plate work-ing life, reduces production costs; The conduction hangers is done the insulation coating near the surface of negative plate main body and is handled, and prevents that hangers is corroded, because the cathode main body is separated making with hangers, has reduced the surface insulation layer coated area, has reduced processing cost.
Description of drawings
Fig. 1 is electrolytic copper powder negative plate structure iron;
Wherein each label is: 1-copper cathode sheets main body; 2-conducts electricity hangers; 3-insulation layer part; The 4-current-carrying part; The 5-hangers that insulate; The 6-junction; The 7-busbar; The 8-liquid level; The 9-electrolyzer;
Fig. 2 is the negative plate structure iron of the electrolytic copper powder among the embodiment 1.
Embodiment
Below in conjunction with accompanying drawing and example the utility model is described further.
A kind of electrolytic copper powder negative plate as shown in Figure 1 is made up of copper cathode sheets main body 1, conduction hangers 2 and insulation hangers 5, and described conduction hangers 2 and insulation hangers 5 are positioned at the both sides at negative plate top, are left-right symmetry; Its conduction hangers 2 is divided into insulation layer part 3 and current-carrying part 4 because being coated with insulating layer coating.
Hangers is by being connected with the material rivet or welding with the mode of connection of negative plate main body.
During use, copper cathode sheets main body 1 is put into electrolyzer 9 carry out electrolysis production, copper cathode sheets main body 1 upper limb will be positioned at 1 ~ 2cm under the electrolysis liquid surface 8, and the current-carrying part 4 of conduction hangers 2 contacts with busbar 7.
Embodiment 1
As shown in Figure 2, be in the electrolyzer of 100cm at width, use wide 86cm, the copper coin of high 60cm is as the negative plate main body, negative plate main body upper limb is lower than liquid level of electrolyte 2cm, has eliminated to form the phenomenon that fine and close thing and main body are corroded, and has prolonged negative plate work-ing life; Owing to removed part on the present used negative plate liquid level, under the situation that effectively the electrolysis area is identical, reduce copper consumption and the weight of negative plate simultaneously, reduced cost, alleviated labour intensity.The conduction hangers is made of copper coin, and copper plate thickness is 1.4cm, and coating part is inverted "L" shaped, and its vertical part is long to be 23cm, and parallel portion is long to be 12cm, and parallel portion is wide to be 5cm, and the insulation layer area of coating has only 0.0384m
2Hangers adopts copper rivet to be connected with the negative plate main body, and when needing to change negative plate like this, hangers is reusable, when perhaps hangers has damage, can change hangers separately.
Claims (2)
1. an electrolytic copper powder negative plate is characterized in that, is made up of copper cathode sheets main body (1), conduction hangers (2) and insulation hangers (5), and described conduction hangers (2) and insulation hangers (5) are positioned at the both sides at negative plate top, are left-right symmetry; Described conduction hangers (2) is divided into insulation layer part (3) and current-carrying part (4) because being coated with insulating layer coating.
2. a kind of electrolytic copper powder negative plate according to claim 1 is characterized in that, hangers is by being connected with the material rivet or welding with the mode of connection of negative plate main body.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220726675 CN203128675U (en) | 2012-12-25 | 2012-12-25 | Cathode plate for electrolytic copper powder |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220726675 CN203128675U (en) | 2012-12-25 | 2012-12-25 | Cathode plate for electrolytic copper powder |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203128675U true CN203128675U (en) | 2013-08-14 |
Family
ID=48936671
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220726675 Expired - Lifetime CN203128675U (en) | 2012-12-25 | 2012-12-25 | Cathode plate for electrolytic copper powder |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203128675U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105063667A (en) * | 2015-08-11 | 2015-11-18 | 深圳崇达多层线路板有限公司 | Cathode plate for electrolysis cell of copper recovery machine, and electrolysis cell |
| CN107130266A (en) * | 2017-06-16 | 2017-09-05 | 江西铜业股份有限公司 | The cathode for electrolyzing plate and preparation method on a kind of band coating side |
-
2012
- 2012-12-25 CN CN 201220726675 patent/CN203128675U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105063667A (en) * | 2015-08-11 | 2015-11-18 | 深圳崇达多层线路板有限公司 | Cathode plate for electrolysis cell of copper recovery machine, and electrolysis cell |
| CN107130266A (en) * | 2017-06-16 | 2017-09-05 | 江西铜业股份有限公司 | The cathode for electrolyzing plate and preparation method on a kind of band coating side |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105154914A (en) | Preparation method of carbon fiber composite anode material | |
| CN201981264U (en) | Cathode carbon block assembly for reducing horizontal current of aluminum liquid layer of electrolytic bath | |
| CN205398745U (en) | Electrodeposition is with electrically conductive head of novel complex | |
| CN203128675U (en) | Cathode plate for electrolytic copper powder | |
| CN201313947Y (en) | Titanium anode device used for electrodeposited metal in hydrometallurgy | |
| CN204385304U (en) | Dipolar four-contact electric conduction device between embedded electrodeposition electrolyzer | |
| CN204307721U (en) | Wet type plate type electrostatic deduster electroconductive frp polar plate device | |
| CN102534667B (en) | Reduce method and the cathode block assembly of horizontal current of aluminum liquid layer of electrolytic bath | |
| CN204265867U (en) | A kind of high-strength electrolytic zinc anode plate | |
| CN204111886U (en) | A kind of insoluble anode plate | |
| CN203639589U (en) | Electroplating device for double-anode double-rectifier system of acid zinc-nickel alloy | |
| CN108630901A (en) | Pole group manufacturing method of the lead-acid accumulator based on sheath copper bus-bar | |
| CN209010620U (en) | Cupric electrolysis cathode collector bar | |
| CN203065588U (en) | Electrolytic anode plate row | |
| CN207845807U (en) | A kind of novel conductive row | |
| CN201864787U (en) | Energy-saving cathode plate for wet-process metallurgy | |
| CN207143356U (en) | Strap electroplating line electroplating conductive device | |
| CN204841955U (en) | Nonmetal electrically conductive polar plate of wet process electric precipitation | |
| CN106319577A (en) | Energy-saving and environment-friendly anode plate | |
| CN202865378U (en) | Electroplating polar plate for coating by pyrolytic process | |
| CN205347602U (en) | Electrodeposition is U type cylinder tubular water -cooling anode plate for metal | |
| CN205295501U (en) | Novel conductive copper bar device | |
| CN104562091A (en) | Embedded type electrodeposition two-pole and four-contact conducting device in electrolytic cell | |
| CN202047150U (en) | Bus belt washing device | |
| CN205188454U (en) | Electrolysis cell |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 100088, 2, Xinjie street, Beijing, Beijing, Xicheng District Co-patentee after: Youyan Powder New Materials Co.,Ltd. Patentee after: GENERAL Research Institute FOR NONFERROUS METALS Address before: 100088, 2, Xinjie street, Beijing, Beijing, Xicheng District Co-patentee before: GRIPM ADVANCED MATERIALS Co.,Ltd. Patentee before: General Research Institute for Nonferrous Metals |
|
| CP01 | Change in the name or title of a patent holder | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190725 Address after: 101407 Beijing city Huairou District Yanqi Yanqi Economic Development Zone South four Street No. 12 Patentee after: Youyan Powder New Materials Co.,Ltd. Address before: 100088, 2, Xinjie street, Beijing, Beijing, Xicheng District Co-patentee before: Youyan Powder New Materials Co.,Ltd. Patentee before: General Research Institute for Nonferrous Metals |
|
| TR01 | Transfer of patent right | ||
| CX01 | Expiry of patent term |
Granted publication date: 20130814 |
|
| CX01 | Expiry of patent term |