CN202576587U - Novel recovery plant of electrolytic gold solution - Google Patents
Novel recovery plant of electrolytic gold solution Download PDFInfo
- Publication number
- CN202576587U CN202576587U CN 201220097315 CN201220097315U CN202576587U CN 202576587 U CN202576587 U CN 202576587U CN 201220097315 CN201220097315 CN 201220097315 CN 201220097315 U CN201220097315 U CN 201220097315U CN 202576587 U CN202576587 U CN 202576587U
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- China
- Prior art keywords
- gold
- electrolysis
- switch
- control panel
- electrolytic
- 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 - Fee Related
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- 239000010931 gold Substances 0.000 title claims abstract description 51
- 229910052737 gold Inorganic materials 0.000 title claims abstract description 51
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 title claims abstract description 50
- 238000011084 recovery Methods 0.000 title claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 43
- 238000005868 electrolysis reaction Methods 0.000 claims description 51
- 206010023126 Jaundice Diseases 0.000 claims description 21
- 238000009423 ventilation Methods 0.000 claims description 3
- 230000005518 electrochemistry Effects 0.000 abstract description 2
- 238000000605 extraction Methods 0.000 abstract description 2
- 229910000510 noble metal Inorganic materials 0.000 abstract 1
- 239000010970 precious metal Substances 0.000 description 12
- 239000007788 liquid Substances 0.000 description 8
- 239000002699 waste material Substances 0.000 description 7
- 238000000034 method Methods 0.000 description 6
- 229910052751 metal Inorganic materials 0.000 description 3
- 239000002184 metal Substances 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 241000416536 Euproctis pseudoconspersa Species 0.000 description 1
- BQCADISMDOOEFD-UHFFFAOYSA-N Silver Chemical compound [Ag] BQCADISMDOOEFD-UHFFFAOYSA-N 0.000 description 1
- 238000003723 Smelting Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000009713 electroplating Methods 0.000 description 1
- 238000005363 electrowinning Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 238000007790 scraping Methods 0.000 description 1
- 229910052709 silver Inorganic materials 0.000 description 1
- 239000004332 silver Substances 0.000 description 1
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- Electrolytic Production Of Metals (AREA)
Abstract
The utility model relates to the technical field of electrochemistry, in particular to the technical field of electrolytic recovery systems, and specifically a noble metal electrolytic recovery system device. The novel recovery plant of the electrolytic gold solution is characterized in that a control panel is arranged at the top end of an electrolytic machine groove, the control panel is provided with a current and voltage display screen, current fine and coarse tuning buttons, voltage fine and coarse tuning buttons, a power switch, a gold recovery switch, a water pump switch and a gold withdrawing switch according to corresponding positions; a water inlet pipe is arranged on one side of the electrolytic machine groove, the water inlet pipe is connected with two mouths, and the two mouths are respectively communicated with a 100 L water inlet valve and a 20 L water inlet valve; a 100 L water outlet valve and a 20 L water outlet valve are arranged on the other side of the electrolytic machine groove; a cathode strip is arranged on the inner side below the control panel of the electrolytic machine groove, and the cathode strip is embedded with a cathode plate. The recovery plant, provided by the utility model, has the characteristics of simple structure, simple operation, semiautomatic button press, high recovery efficiency, no pollution, high purity of gold obtained by electrolytic extraction, high efficiency and the like.
Description
Technical field
The utility model relates to technical field of electrochemistry, and particularly the electrolyzing and recycling system technical field specifically is meant a kind of precious metal electrolyzing and recycling system equipment.
Background technology
People in industry knows in the exploitation, smelting, use of precious metals such as gold and silver, palladium, can produce the multiple waste liquid that contains precious metal inevitably.Particularly electronics manufacturing is to the continuous increase of precious metal demand, usage quantity owing to modern industry, and the contracts amount that causes containing the precious metal waste liquid is also in continuous growth.In addition, the stop bath of hospital, photo studio, and the electroplating effluent of Electroplate Factory all are the important sources that contains the precious metal waste liquid.Because the precious metal in the waste liquid has high economic worth, so each research institution and enterprise all are devoted to develop the technology of extraction precious metal from contain the precious metal waste liquid.The Rare Metals process for extracting mainly contains chemical method and electrolytic process etc. at present, yet chemical method reduces gradually in recent years and uses because pollution is comparatively serious.
At present, electrolytic process is used widely in each metal recovery enterprise because it has recovery height, produces characteristics such as pollution is low, recovery metal purity height.Meanwhile, each waste liquid manufacturer also recognizes the value that contains the precious metal waste liquid gradually, the autonomous precious metal that extracts of beginning.
Summary of the invention
In order to solve the above problems, the purpose of the utility model provides a kind of novel electrolysis precious metal solution equipment, especially electrolysis gold solution.
In order to reach above-mentioned purpose; Technical scheme below the utility model has adopted: a kind of recovery system of novel electrolysis gold solution; Mainly comprise: the current/voltage image display; The little coarse adjustment button of electric current; The little coarse adjustment button of voltage; Power switch; Gold reclaims switch; Pump switch; Removing jaundice gold switch; Cathode strip; Negative plate; Positive plate; Fan; Power interface; Water inlet pipe; The 100L water intaking valve; The 20L water intaking valve; The removing jaundice gold anode; The removing jaundice gold anode; The 100L water discharge valve; The 20L outlet valve; Adjustable under-chassis; The electrolysis trough; Control panel
Described electrolysis trough top is provided with control panel, is provided with current/voltage image display, the little coarse adjustment button of electric current, the little coarse adjustment button of voltage, power switch, gold recovery switch, pump switch, removing jaundice gold switch according to corresponding position on the control panel;
Electrolysis trough one side is provided with water inlet pipe, and water inlet pipe is connected to two opennings, and it is connected with 100L water intaking valve and 20L inlet valve respectively;
Electrolysis trough opposite side is provided with 100L water discharge valve and 20L outlet valve;
The inboard is provided with cathode strip under the electrolysis trough control panel, is inlaid with negative plate on the cathode strip; The inboard the other side of electrolysis trough is provided with positive plate;
Electrolysis trough inboard also is provided with removing jaundice gold anode and removing jaundice gold anode.
Also be provided with water pump in the above-mentioned electrolysis trough.
Above-mentioned electrolysis trough shell one place is provided with power interface, and the control panel ventilation also is provided with fan.
Above-mentioned electrolysis machine bottom land end also is provided with liftable adjustable under-chassis.
Above-mentioned negative plate, the electrolysis voltage between the positive plate are 2 V ~ 2.4V; Electrolysis time is 16h ~ 18h.
The beneficial effect of the utility model: device structure is simple, and is easy and simple to handle.Button is semi-automatic, organic efficiency is high, do not produce pollution.Characteristics such as the fineness of gold height of electrowinning, efficient height.
Description of drawings
Fig. 1 is the structural representation of the recovery system of a kind of novel electrolysis gold solution of the utility model.
Fig. 2 is embedded in the synoptic diagram on the cathode strip for the utility model negative plate.
1-current/voltage image display among the figure; The little coarse adjustment button of 2-electric current; The little coarse adjustment button of 3-voltage; The 4-power switch; 5-gold reclaims switch; The 6-pump switch; 7-removing jaundice gold switch; The 8-cathode strip; The 9-negative plate; The 10-positive plate; The 11-fan; The 12-power interface; The 13-water inlet pipe; The 14-100L water intaking valve; The 15-20L water intaking valve; 16-removing jaundice gold anode; 17-removing jaundice gold anode; The 18-100L water discharge valve; The 19-20L outlet valve; The adjustable under-chassis of 20-; 21-electrolysis trough; The 22-control panel.
Embodiment
Below in conjunction with accompanying drawing 1-2 the embodiment of the utility model is done a detailed explanation.
Embodiment: a kind of recovery system of novel electrolysis gold solution; Mainly comprise: current/voltage image display 1; The little coarse adjustment button 2 of electric current; The little coarse adjustment button 3 of voltage; Power switch 4; Gold reclaims switch 5; Pump switch 6; Removing jaundice gold switch 7; Cathode strip 8; Negative plate 9; Positive plate 10; Fan 11; Power interface 12; Water inlet pipe 13; 100L water intaking valve 14; 20L water intaking valve 15; Removing jaundice gold anode 16; Removing jaundice gold anode 17; 100L water discharge valve 18; 20L outlet valve 19; Adjustable under-chassis 20; Electrolysis trough 21; Control panel 22
Described electrolysis trough 21 tops are provided with control panel 22, are provided with the little coarse adjustment button of the little coarse adjustment button of current/voltage image display 1, electric current 2, voltage 3, power switch 4, gold according to corresponding position on the control panel 22 and reclaim switch 5, pump switch 6, removing jaundice gold switch 7;
22 times inboards of electrolysis trough 21 control panels are provided with cathode strip 8, are inlaid with negative plate 9 on the cathode strip 8; Electrolysis trough 21 inboard the other sides are provided with positive plate 10;
Also be provided with water pump in the described electrolysis trough 21.
Described electrolysis trough 21 shells one place is provided with power interface 12, and control panel 22 ventilations also are provided with fan 11.
Described electrolysis trough 21 bottoms also are provided with liftable adjustable under-chassis 20.
Electrolysis voltage between described negative plate 9, the positive plate 10 is 2 V ~ 2.4V; Electrolysis time is 16h ~ 18h.
Take a detailed example to an implementation process below:
If the gold liquor capacity greater than 22L, is closed 20L water intaking valve 15 earlier, after open 100L water intaking valve 14; If the gold liquor capacity less than 22L, is opened 20L water intaking valve 15 earlier, after close 100L water intaking valve 14.
The solution that will contain gold is again poured in the electrolysis trough 21, turns on the power switch 4, gold reclaims switch 5, device start.Regulate the little coarse adjustment button of pump switch 6 and electric current 2, the little coarse adjustment button of voltage this moment, 3 are adjusted to 2.2V with voltage, after one hour, will be adjusted into 2.4V again, stablize electrolysis 17 hours with this voltage.
After waiting to contain the complete electrolysis of solution of gold, negative plate 9 is taken off from cathode strip 8, water rinsing gently then, residual chemical medicinal liquid composition above the removal is adsorbed on the negative plate 9 at last and presents spongiform gold and scrapes with cutter.
Spongy gold after scraping is collected in together, pours crucible into behind the oven dry moisture, and calcination becomes ingot.
Claims (5)
1. the recovery system of a novel electrolysis gold solution; Mainly comprise: current/voltage image display (1); The little coarse adjustment button of electric current (2); The little coarse adjustment button of voltage (3); Power switch (4); Gold reclaims switch (5); Pump switch (6); Removing jaundice gold switch (7); Cathode strip (8); Negative plate (9); Positive plate (10); Fan (11); Power interface (12); Water inlet pipe (13); 100L water intaking valve (14); 20L water intaking valve (15); Removing jaundice gold anode (16); Removing jaundice gold anode (17); 100L water discharge valve (18); 20L outlet valve (19); Adjustable under-chassis (20); Electrolysis trough (21); Control panel (22)
It is characterized in that: electrolysis trough (21) top is provided with control panel (22), and control panel (22) is gone up according to corresponding position and is provided with current/voltage image display (1), the little coarse adjustment button of electric current (2), the little coarse adjustment button of voltage (3), power switch (4), gold recovery switch (5), pump switch (6), removing jaundice gold switch (7);
Electrolysis trough (21) one sides are provided with water inlet pipe (13), and water inlet pipe (13) is connected to two opennings, and it is connected with 100L water intaking valve (14) and 20L inlet valve (15) respectively;
Electrolysis trough (21) opposite side is provided with 100L water discharge valve (18) and 20L outlet valve (19);
Electrolysis trough (21) control panel (22) is provided with cathode strip (8) in the inboard down, is inlaid with negative plate (9) on the cathode strip (8); The inboard the other side of electrolysis trough (21) is provided with positive plate (10);
Electrolysis trough (21) inboard also is provided with removing jaundice gold anode (16) and removing jaundice gold anode (17).
2. the recovery system of a kind of novel electrolysis gold solution according to claim 1 is characterized in that also being provided with water pump in the described electrolysis trough (21).
3. the recovery system of a kind of novel electrolysis gold solution according to claim 1 is characterized in that described electrolysis trough (21) shell one place is provided with power interface (12), and control panel (22) ventilation also is provided with fan (11).
4. the recovery system of a kind of novel electrolysis gold solution according to claim 1 is characterized in that described electrolysis trough (21) bottom also is provided with liftable adjustable under-chassis (20).
5. the recovery system of a kind of novel electrolysis gold solution according to claim 1 is characterized in that the electrolysis voltage between described negative plate (9), the positive plate (10) is 2 V ~ 2.4V; Electrolysis time is 16h ~ 18h.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220097315 CN202576587U (en) | 2012-03-15 | 2012-03-15 | Novel recovery plant of electrolytic gold solution |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 201220097315 CN202576587U (en) | 2012-03-15 | 2012-03-15 | Novel recovery plant of electrolytic gold solution |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN202576587U true CN202576587U (en) | 2012-12-05 |
Family
ID=47246017
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 201220097315 Expired - Fee Related CN202576587U (en) | 2012-03-15 | 2012-03-15 | Novel recovery plant of electrolytic gold solution |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN202576587U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114182300A (en) * | 2021-12-24 | 2022-03-15 | 福建省福联集成电路有限公司 | Equipment for recovering gold by chemical electrolysis and using method thereof |
-
2012
- 2012-03-15 CN CN 201220097315 patent/CN202576587U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114182300A (en) * | 2021-12-24 | 2022-03-15 | 福建省福联集成电路有限公司 | Equipment for recovering gold by chemical electrolysis and using method thereof |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| ASS | Succession or assignment of patent right |
Owner name: ZHANG ZHEN Free format text: FORMER OWNER: ZHUANG YUEJIAN Effective date: 20121204 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| C53 | Correction of patent for invention or patent application | ||
| CB03 | Change of inventor or designer information |
Inventor after: Zhang Zhen Inventor before: Zhuang Yuejian |
|
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 518017 SHENZHEN, GUANGDONG PROVINCE TO: 415101 CHANGDE, HUNAN PROVINCE Free format text: CORRECT: INVENTOR; FROM: ZHUANG YUEJIAN TO: ZHANG ZHEN |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20121204 Address after: 415101, No. 35, Station Lane, Wuling Town, Dingcheng District, Hunan, Changde Patentee after: Zhang Zhen Address before: 518017 No. 274, Shui Wai village, Shenzhen, Guangdong, Futian District Patentee before: Zhuang Yuejian |
|
| ASS | Succession or assignment of patent right |
Owner name: JIANGXI SAIYUN HIGH-TECH CO., LTD. Free format text: FORMER OWNER: ZHANG ZHEN Effective date: 20131018 |
|
| C41 | Transfer of patent application or patent right or utility model | ||
| COR | Change of bibliographic data |
Free format text: CORRECT: ADDRESS; FROM: 415101 CHANGDE, HUNAN PROVINCE TO: 341699 GANZHOU, JIANGXI PROVINCE |
|
| TR01 | Transfer of patent right |
Effective date of registration: 20131018 Address after: 341699 Jiangxi Province, Ganzhou City Yingbin Avenue South jingjiangshan District 2 room 507 Patentee after: Jiangxi MC High Technology Co., Ltd. Address before: 415101, No. 35, Station Lane, Wuling Town, Dingcheng District, Hunan, Changde Patentee before: Zhang Zhen |
|
| C17 | Cessation of patent right | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20121205 Termination date: 20140315 |