CN203346485U - Precious metal recovery electrolyzer - Google Patents
Precious metal recovery electrolyzer Download PDFInfo
- Publication number
- CN203346485U CN203346485U CN201320339594XU CN201320339594U CN203346485U CN 203346485 U CN203346485 U CN 203346485U CN 201320339594X U CN201320339594X U CN 201320339594XU CN 201320339594 U CN201320339594 U CN 201320339594U CN 203346485 U CN203346485 U CN 203346485U
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- waste liquid
- liquid reaction
- electrolyzer
- plate
- reaction zone
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/20—Recycling
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Abstract
The utility model provides a precious metal recovery electrolyzer which comprises a shell, a circulating pump, a waste liquid reaction area and a current control device, wherein the circulating pump and the waste liquor reaction area are arranged in the shell, a liquid inlet and a liquid outlet are arranged in the waste liquid reaction area, the circulating pump is connected with the liquid inlet in the waste liquid reaction area, the waste liquid reaction area is internally provided with an anode plate and a cathode plate, and the anode plate and the cathode plate are respectively electrically connected with the current control device. The precious metal recovery electrolyzer has the benefits that the functions are added, the defect of liquid leakage is overcome, the structure is simplified, the precious metal recovery electrolyzer is easy to manufacture and convenient to operate, low in fault rate, safe and reliable as well as environmentally friendly, saves energy, the parts are simple to manufacture, the production rate is greatly increased, and the production cost is lowered.
Description
Technical field
The utility model relates to the metal recovery unit field, especially relates to a kind of noble metal and reclaims electrolyzer, is applicable to the recovery containing gold in golden waste liquid.
Background technology
Existing noble metal reclaims electrolyzer and generally adopts the combination of titanium bucket and positive plate, the waste liquid that will contain noble metal is positioned in the titanium bucket, utilize different metal element eletrolyzable principle under different electric current and voltage effects that the metallic element in waste liquid is electroplated onto on the titanium bucket, but there is very large deficiency in above-mentioned technology.The deficiency existed has: structure is too simplified, the part processing difficulties, and adjustment is wasted time and energy, and working efficiency is too low, and when the too dirty impurity of waste liquid is too many, the too little liquid of the volume of reaction unit is understood the technical problems such as excessive.
Summary of the invention
The purpose of this utility model is to provide a kind of a kind of noble metal simple in structure, simple to operate, that production efficiency is high and reclaims electrolyzer.
The technical solution of the utility model is: a kind of noble metal reclaims electrolyzer, comprise shell, recycle pump, waste liquid reaction zone and current control device, described recycle pump and described waste liquid reaction zone are arranged in described shell, be provided with fluid inlet and liquid outlet on described waste liquid reaction zone, and described recycle pump is connected with the described fluid inlet of described waste liquid reaction zone, be provided with positive plate and negative plate in described waste liquid reaction zone, and described positive plate and described negative plate are electrically connected to described current control device respectively.The Whole Equipment compactness, save space, and flow by waste liquid by recycle pump, and reaction is occurred in this limited area of waste liquid reaction zone, greatly improved throughput rate, reduced production cost.
Further, described waste liquid reaction zone top is provided with top cover, and described positive plate is connected with described top cover with described negative plate.When dismounting titanium plate, only the top cover removed on the waste liquid reaction zone need be come, the power supply connected on the titanium plate is pulled down, the titanium plate can be taken down, be easy to adjust and change, increase work efficiency.
Further, it is some right that described positive plate and described negative plate are provided with, and described positive plate and described negative plate are the space discharge.Multiple plating, increase work efficiency.
Further, the level attitude of described fluid inlet is lower than the level attitude with described liquid outlet.When device work, remain a certain amount of waste liquid in the waste liquid reaction zone, and the waste liquid circulation thoroughly, do not have waste liquid residual, affects electroplating effect.
Further, described negative plate is the titanium plate, and described positive plate is titanium base iridium dioxide plate.Adopt titanium base iridium dioxide as the sacrificial metal material, its expendable is little, and can improve electrolytic reduction efficiency, shortens electrolysis time.
Further, the material of described waste liquid reaction zone is the PP material.Material capability is stable, with waste liquid, does not produce and reacts.
Advantage and the positively effect that the utlity model has are: owing to adopting technique scheme, the beneficial effect determined by structure of the present utility model has increased function, has overcome the shortcoming of leakage, has simplified the structure, has been easy to manufacture, failure rate is low, safe and reliable, energy-conserving and environment-protective, convenient operation, part processing have improved throughput rate simply, greatly, reduced production cost.
The accompanying drawing explanation
Fig. 1 is structural representation of the present utility model;
Fig. 2 is the cross-sectional schematic of waste liquid reaction zone.
In figure:
1, shell 2, recycle pump 3, waste liquid reaction zone
4, current control device 5, fluid inlet 6, liquid outlet
7, positive plate 8, negative plate 9, top cover
Embodiment
As shown in Figure 1, the utility model comprises long 100cm, the shell 1 of the box profile of wide 80cm, be arranged on recycle pump 2 and the waste liquid reaction zone 3 that adopts the PP material in shell 1 fully, be provided with fluid inlet 5 and liquid outlet 6 on described waste liquid reaction zone 3, and described recycle pump 2 is connected with the described fluid inlet 5 of described waste liquid reaction zone 3, between being provided with in described waste liquid reaction zone 3 across the use titanium base iridium dioxide plate of discharge as the positive plate 7 of sacrificial metal with use the negative plate 8 of titanium plate as reducing metal, i.e. 7 negative plates 8 of a positive plate, positive plate 7 negative plate 8 order discharges more again, and described positive plate 7 and described negative plate 8 are electrically connected to described current control device 4 respectively, negative plate 8 and positive plate 7 be connecting to neutral line and live wire respectively, form electric power loop during energising, described waste liquid reaction zone 3 tops are provided with the top cover 9 of PP material, from each negative plate 8 and positive plate 7, draw on the top cover 9 of a rod insertion pp material, by screw locking, negative plate 8 and positive plate 7 all have the nut of PP material and plastic cement pad that they are locked, in order to avoid waste liquid leakage from the mouth of the connection rod of negative plate 8 and positive plate 7 is introversive, the level attitude of described fluid inlet 5, lower than the level attitude with described liquid outlet 6.
The working process of this example: a pipe is installed in the water inlet at recycle pump, also connect a pipe at liquid outlet simultaneously, two tubes is placed in the ton bucket that waste liquid is housed, by recycle pump, waste liquid is extracted into to the waste liquid reaction zone of pp material, with this method, waste liquid is circulated.Make waste liquid form water cycle completely, also the bubble in electrolyzer can be driven away, in order to avoid the electrolyzer internal cause has bubble, dally electrolyzer is burnt out simultaneously, opening power, adjust current/voltage to required numerical value, check whether each interface leaks, and electrolyzer just starts normal operation.Detect the content of residual waste solution in the ton bucket every day, when content reaches desired data when following, close the electrolyzer power supply, after pump to be recycled lets cool, just can pull down negative plate, during the dismounting negative plate, only the waste liquid reaction zone upper cover of PP material need be removed, the power supply connected on negative plate is removed and gets final product, then negative plate is dried and weighed, after carrying out, required operation gets final product.
Above an embodiment of the present utility model is had been described in detail, but described content is only preferred embodiment of the present utility model, can not be considered to for limiting practical range of the present utility model.All equalization variations of doing according to the utility model application range and improvement etc., within all should still belonging to patent covering scope of the present utility model.
Claims (6)
1. a noble metal reclaims electrolyzer, it is characterized in that: comprise shell, recycle pump, waste liquid reaction zone and current control device, described recycle pump and described waste liquid reaction zone are arranged in described shell, be provided with fluid inlet and liquid outlet on described waste liquid reaction zone, and described recycle pump is connected with the described fluid inlet of described waste liquid reaction zone, be provided with positive plate and negative plate in described waste liquid reaction zone, and described positive plate and described negative plate are electrically connected to described current control device respectively.
2. a kind of noble metal according to claim 1 reclaims electrolyzer, and it is characterized in that: described waste liquid reaction zone top is provided with top cover, and described positive plate is connected with described top cover with described negative plate.
3. a kind of noble metal according to claim 1 reclaims electrolyzer, and it is characterized in that: it is some right that described positive plate and described negative plate are provided with, and described positive plate and described negative plate are the space discharge.
4. a kind of noble metal according to claim 1 reclaims electrolyzer, and it is characterized in that: the level attitude of described fluid inlet is lower than the level attitude with described liquid outlet.
5. a kind of noble metal according to claim 1 reclaims electrolyzer, and it is characterized in that: described negative plate is the titanium plate, and described positive plate is titanium base iridium dioxide plate.
6. a kind of noble metal according to claim 1 reclaims electrolyzer, and it is characterized in that: the material of described waste liquid reaction zone is the PP material.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320339594XU CN203346485U (en) | 2013-06-13 | 2013-06-13 | Precious metal recovery electrolyzer |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201320339594XU CN203346485U (en) | 2013-06-13 | 2013-06-13 | Precious metal recovery electrolyzer |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203346485U true CN203346485U (en) | 2013-12-18 |
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ID=49746407
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201320339594XU Expired - Fee Related CN203346485U (en) | 2013-06-13 | 2013-06-13 | Precious metal recovery electrolyzer |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203346485U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107034485A (en) * | 2017-06-14 | 2017-08-11 | 北京川金环保科技有限公司 | A kind of novel environment friendly quick separating reclaims precious metal ion device product |
-
2013
- 2013-06-13 CN CN201320339594XU patent/CN203346485U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107034485A (en) * | 2017-06-14 | 2017-08-11 | 北京川金环保科技有限公司 | A kind of novel environment friendly quick separating reclaims precious metal ion device product |
| CN107034485B (en) * | 2017-06-14 | 2019-04-05 | 张镇 | A kind of environmental protection quick separating recycling precious metal ion device product |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20131218 Termination date: 20150613 |
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| EXPY | Termination of patent right or utility model |