CN204589329U - For the electrolysis triplicate form body module that precious metal is purified - Google Patents
For the electrolysis triplicate form body module that precious metal is purified Download PDFInfo
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- CN204589329U CN204589329U CN201520192110.2U CN201520192110U CN204589329U CN 204589329 U CN204589329 U CN 204589329U CN 201520192110 U CN201520192110 U CN 201520192110U CN 204589329 U CN204589329 U CN 204589329U
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- form body
- triplicate form
- triplicate
- electrolysis
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- Electrolytic Production Of Metals (AREA)
Abstract
For the electrolysis triplicate form body module that precious metal is purified, it mainly comprises triplicate form body, support, described support is one can hold and install the integral support structure of multiple triplicate form body, and the triplicate form body in integral support structure is arranged in order with the left and right sides and is formed two row's arrangements, integral support structure connects triplicate form body by supporting circulation line; Described triplicate form body is vertically mounted on support, is installed to be connected and fixed to form by three cell bodies by upper connectors and bottom junctor, and described cell body inside is containing anode and negative electrode; Wear ring is installed above described upper connectors successively, triplicate form body that gland, upper end cover form a sealing; Described bottom junctor is provided with electrolytic solution and sends into mouth, and be communicated with electrolytic solution storage container by this feeding mouth; It has, and structure composition is reasonable, compact, easy to use and reliable, easy for installation, and use range is wide, greatly can reduce the features such as investment and production cost.
Description
Technical field
The utility model relates to a kind of electrolysis triplicate form body module of purifying for precious metal, belong to the technical field of resource circulation utilization equipment.
Background technology
Traditional electrolysis tech anode and cathode is placed in the cell body of sluggish flow or stagnation, under the effect of electric field, negatively charged ion anode displacement, positively charged ion is to negative electrode displacement, by controlling certain technical qualification, metallic cation for obtaining obtains electronic deposition at negative electrode and separates out, thus obtains electrolytic metal product.When target metal ions concentration is lower, easily there is the concentration polarization phenomenon of negative electrode in traditional electrodeposition technology, causes a small amount of foreign ion to separate out on negative electrode together with target metal ions, cause cathode product quality degradation.
In recent years, the development of refining precious metal technology, it is the difference based on the theoretical deposition potential of each metal ion, as long as the metal namely for being extracted has larger potential difference with other metal ions in solution system, then the metal of current potential calibration is easy to preferentially separate out at negative electrode, and its key eliminates the disadvantageous effect to electrolysis such as concentration polarization by high velocity liquid stream.But also have problems at present, do not apply on a large scale.
Therefore, promote precious metal purification electrolysis technology further, adopt rational electrolyzer structure formation, effectively absorb target metal ions, to obtaining further, high purity electrolytic metal product is significant.
Summary of the invention
The purpose of this utility model is the deficiency overcoming prior art existence, a kind of structure is provided to form reasonable, compact, easy to use and reliable, easy for installation, by improving the cathode area of electrolyzer, further increase the efficiency of electrolysis, thus reduce the electrolysis triplicate form body module of purifying for precious metal of power consumption.
The purpose of this utility model has been come by following technical solution, a kind of electrolysis triplicate form body module of purifying for precious metal, it mainly comprises triplicate form body, support, described support is one can hold and install the integral support structure of multiple triplicate form body, and the triplicate form body in integral support structure is arranged in order with the left and right sides and is formed two row's arrangements, integral support structure connects triplicate form body by supporting circulation line;
Described triplicate form body is vertically mounted on support, is installed to be connected and fixed to form by three cell bodies by upper connectors and bottom junctor, and described cell body inside is provided with anode and negative electrode.
Wear ring is installed above upper connectors of the present invention successively, triplicate form body that gland, upper end cover form a sealing; Described bottom junctor is provided with electrolytic solution and sends into mouth, and be communicated with electrolytic solution storage container by this feeding mouth.
Wear ring of the present invention be made up of rubber and each cell body to there being a wear ring; Described upper end cover seals triplicate form body by rotatably compressing gland, and upper end cover is made up of corrosion-resistant engineering plastics injection moulding;
Described cell body metal titanium is made, and wall thickness is 3-6mm; The anode of described cell body inside is made for being coated with SC3 outward by copper titanium composite base material; Described wear ring, gland, upper end cover are all made up of nonconducting engineering plastics injection moulding.
The groove monolithic design of electrolysis is mainly tri-coupling type arrangement by the utility model, effectively can improve cathode area and the electrolytic efficiency thereof of electrolyzer.
The production that the utility model is mainly used in carrying out copper, cobalt, nickel, zinc, gold and silver, platinum and other valuable metal in all kinds of acid system and recovery, being separated and the process of heavy metal ion-containing waste water of hybrid metal solution, all can reach higher metal recovery rate.
The utility model has following obviously beneficial effect: the groove of electrolysis is designed to triplicate form body formula arranged in parallel, effectively can improves the cathode area of electrolyzer, further increase the efficiency of electrolysis, thus reduce power consumption; Catholyte metal product can several electrolysis monomer feeding simultaneously after electrolysis completes for module, convenient and swift; It has, and structure composition is reasonable, compact, easy to use and reliable, easy for installation, and use range is wide, greatly can reduce the features such as investment and production cost.
Accompanying drawing explanation
Fig. 1 is electrolysis triplicate form body and the module schematic diagram thereof of the purification of the utility model precious metal.
Fig. 2 is the electrolysis triplicate form body schematic diagram that the utility model precious metal is purified.
Fig. 3 is the electrolysis triplicate form body layering schematic diagram that the utility model precious metal is purified.
Fig. 4 is the electrolysis triplicate form body upper end cover schematic diagram that the utility model precious metal is purified.
Fig. 5 is the electrolysis triplicate form body gland schematic diagram that the utility model precious metal is purified.
Fig. 6 is the electrolysis triplicate form body upper connectors schematic diagram that the utility model precious metal is purified.
Embodiment
Drawing reference numeral illustrates: triplicate form body 1, support 2, upper end cover 11, gland 12, wear ring 13, upper connectors 14, anode 15, cell body 16, negative electrode 17, bottom junctor 18.
Below in conjunction with accompanying drawing, the utility model is further described: shown in Fig. 1-3, a kind of electrolysis triplicate form body module of purifying for precious metal described in the utility model, it mainly comprises triplicate form body 1, support 2, described support 2 is one can hold and install the integral support structure of multiple triplicate form body 1, and the triplicate form body 1 in integral support structure is arranged in order with the left and right sides and is formed two row's arrangements, integral support structure connects triplicate form body 1 by supporting circulation line;
Described triplicate form body 1 is vertically mounted on support 2, is installed to be connected and fixed to form by three cell bodies 16 by upper connectors 14 and bottom junctor 18, and described cell body 16 inside is containing anode 15 and negative electrode 17.
Shown in composition graphs 4-6, the triplicate form body 1 that described upper connectors 14 is provided with above wear ring 13 successively, gland 12, upper end cover 11 form a sealing; Described bottom junctor 18 is provided with electrolytic solution and sends into mouth, and be communicated with electrolytic solution storage container by this feeding mouth.
Described wear ring 13 is made up of rubber, and each cell body 16 is to there being a wear ring 13; Described upper end cover 11 seals triplicate form body 1 by rotatably compressing gland, and upper end cover 11 is made up of corrosion-resistant engineering plastics injection moulding;
Described cell body 16 is made with metal titanium, and wall thickness is 3-6mm; The anode of described cell body 16 inside is made for being coated with SC3 outward by copper titanium composite base material; Described wear ring 13, gland 12, upper end cover 11 are all made up of nonconducting engineering plastics injection moulding.
Embodiment: for 2 X 4 triplicate form bodies and composition graphs 1-6, description will be described in further detail to the technical solution of the utility model: the utility model mainly contains triplicate form body 1, support 2 forms below.Described support 2, according to 2 X 4 triplicate form body electrolytic systems, is designed to an integral support device, each side fixedly mounts 4 triplicate form bodies 1, and supporting circulation line.
Described triplicate form body 1 at right angle setting, and be made up of three cell bodies 16; Three cell body 16 upper sections of described triplicate form body 1 install upper connectors 14 successively, wear ring 13, gland 12, upper end cover 11 form a hermetic electrolyte device.Described upper connectors 14 and bottom junctor 18 installation are fixed three cell bodies 16 and are formed a triplicate form body 1.
Described cell body 16 material is metal titanium, and wall thickness is 3-6mm; Anode 15 and negative electrode 17 are all contained in described cell body 16 inside.Described anode 15 material is that copper titanium composite base material is coated with SC3 outward.Described wear ring 13, gland 12, upper end cover 11 are all that nonconducting engineering plastics injection moulding is made.
The utility model needs to form electrolytic system at the supporting solution circulated pipeline of connection and solution circulation pump.Electrolyzer in the course of the work solution enters cell body 16 from bottom junctor 18, flow at high speed in cell body, and at negative electrode precipitating metal settling.Bubbing on anode, this gas is collected by the device of electrolysis module and is concentrated laggard row relax.When the metal deposit of negative electrode reaches certainweight time, opening upper end cover 11 above, gland 12, wear ring 13 from top taking-up, after cleaning, from newly adding, wear ring 13, gland 12, upper end cover 11 hermetic electrolyte device continuation cyclic electrolysis being installed.
The utility model is mainly used in all kinds of acid system (sulfuric acid, hydrochloric acid, nitric acid and prussiate etc.), carry out copper, cobalt, nickel, zinc, gold and silver, platinum and other valuable metal production and recovery, the separation of hybrid metal solution and the process etc. of heavy metal ion-containing waste water, be particularly suitable for metallurgy industry to lower concentration, the selective electrolysis isolation andpurification of complicated solution.
Claims (3)
1. for the electrolysis triplicate form body module of precious metal purification, it mainly comprises triplicate form body, support, it is characterized in that described support is one can hold and install the integral support structure of multiple triplicate form body, and the triplicate form body in integral support structure is arranged in order with the left and right sides and is formed two row's arrangements, integral support structure connects triplicate form body by supporting circulation line;
Described triplicate form body is vertically mounted on support, is installed to be connected and fixed to form by three cell bodies by upper connectors and bottom junctor, and described cell body inside is containing anode and negative electrode.
2. electrolysis triplicate form body module of purifying for precious metal according to claim 1, is characterized in that being provided with successively above described upper connectors wear ring, triplicate form body that gland, upper end cover form a sealing; Described bottom junctor is provided with electrolytic solution and sends into mouth, and be communicated with electrolytic solution storage container by this feeding mouth.
3. according to claim 2 for precious metal purify electrolysis triplicate form body module, it is characterized in that described wear ring be made up of rubber and each cell body to there being a wear ring; Described upper end cover seals triplicate form body by rotatably compressing gland, and upper end cover is made up of corrosion-resistant engineering plastics injection moulding;
Described cell body metal titanium is made, and wall thickness is 3-6mm; The anode of described cell body inside is made for being coated with SC3 outward by copper titanium composite base material; Described wear ring, gland, upper end cover are all made up of nonconducting engineering plastics injection moulding.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520192110.2U CN204589329U (en) | 2015-04-01 | 2015-04-01 | For the electrolysis triplicate form body module that precious metal is purified |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201520192110.2U CN204589329U (en) | 2015-04-01 | 2015-04-01 | For the electrolysis triplicate form body module that precious metal is purified |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN204589329U true CN204589329U (en) | 2015-08-26 |
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Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201520192110.2U Withdrawn - After Issue CN204589329U (en) | 2015-04-01 | 2015-04-01 | For the electrolysis triplicate form body module that precious metal is purified |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN204589329U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104775138A (en) * | 2015-04-01 | 2015-07-15 | 马恩高 | Electrolytic triple unit module for purifying noble metal |
-
2015
- 2015-04-01 CN CN201520192110.2U patent/CN204589329U/en not_active Withdrawn - After Issue
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104775138A (en) * | 2015-04-01 | 2015-07-15 | 马恩高 | Electrolytic triple unit module for purifying noble metal |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| AV01 | Patent right actively abandoned |
Granted publication date: 20150826 Effective date of abandoning: 20170322 |
|
| C25 | Abandonment of patent right or utility model to avoid double patenting |