CN205528954U - Copper -containing, nickel heavy metal comprehensive utilization of waste materials system - Google Patents
Copper -containing, nickel heavy metal comprehensive utilization of waste materials system Download PDFInfo
- Publication number
- CN205528954U CN205528954U CN201620075291.5U CN201620075291U CN205528954U CN 205528954 U CN205528954 U CN 205528954U CN 201620075291 U CN201620075291 U CN 201620075291U CN 205528954 U CN205528954 U CN 205528954U
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- CN
- China
- Prior art keywords
- storehouse
- heavy metal
- communicating pipe
- delivery line
- cupric
- 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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- 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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- Manufacture And Refinement Of Metals (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
The utility model discloses a copper -containing, nickel heavy metal comprehensive utilization of waste materials system, soaking including alkali and handling storehouse and alkali and soak the one end of handling the storehouse and be provided with first communicating pipe, the one end intercommunication of first communicating pipe has the ammonia process to handle storehouse and ammonia process to handle the one end in storehouse and be provided with second communicating pipe, and the one end intercommunication of second communicating pipe has collection copper storehouse, one side that the storehouse was handled to the ammonia process is provided with the interpolation pipe, and the one end of adding the pipe is provided with adds the feed bin, one end intercommunication that the one end in collection copper storehouse was provided with first contact tube and first contact tube has an impurity removal and purification storehouse, and the one end intercommunication that the one end in impurity removal and purification storehouse was provided with second contact tube and second contact tube has concentrated crystallization process jar. The utility model discloses a treatment effeciency is high, has improved the efficiency of carrying out metal recycling, the oxidant that adds in adding the feed bin can get into the ammonia process and handles the storehouse through adding the pipe, can make the heavy metal wastes material accomplish furthest's minimizing and innoxious, the efficiency of post processing is improved, simple structure, convenient to use.
Description
Technical field
The utility model relates to a kind of nonferrous metals recycling system, particularly to a kind of cupric, the comprehensive utilization of nickel heavy metal waste is
System.
Background technology
Metal recovery refers to that the utility separated from waste metal becomes regeneration through physics or machining
Goods, are that metal recovery industry defines a complete industrial chain from reclaiming, disassemble, to an industrial chain of regeneration
And the regeneration ecosphere, this industrial chain is from the beginning of external waste material supplier, through trader, importer, agent, port
Mouthful, disassemble factory (designated enterprise or hardware factory), reclaim the link such as company, Metal Processing Factory, it is achieved that effective utilization of resource.
Current metal recovery China develop very rapid, define the most complete industrial chain, but existing have coloured gold
Belong to and reclaim the recovery of especially cupric non-ferrous metal processing when, pending waste metal is processed time
Wait, it is impossible to carry out high efficiency process, reduce the reduction carrying out metal recovery efficiency, and existing cupric non-ferrous metal returns
Receipts system impurity volume of generation carrying out metal recovery when is relatively big and heavy contamination, increases the difficulty that the later stage processes.
Utility model content
The technical problems to be solved in the utility model is the defect overcoming prior art, it is provided that a kind of cupric, nickel heavy metal waste are combined
Conjunction utilizes system.
In order to solve above-mentioned technical problem, the utility model provides following technical scheme:
The utility model one cupric, nickel heavy metal waste utilization system, process storehouse including alkali leaching and described alkali leaching process storehouse
One end be provided with for the first communicating pipe, one end of described first communicating pipe is communicated with ammonia process and processes storehouse and described ammonia process and process the one of storehouse
End was provided with for the second communicating pipe, and one end of described second communicating pipe is communicated with extraction copper storehouse.
As a kind of optimal technical scheme of the present utility model, described ammonia process processes the side in storehouse and is provided with adding tube, described interpolation
One end of pipe is provided with filling storehouse.
As a kind of optimal technical scheme of the present utility model, the one end in described extraction copper storehouse is provided with the first delivery line and described first
One end of delivery line is communicated with impurity and purification storehouse, and the one end in described impurity and purification storehouse is provided with the second delivery line and described second and derives
One end of pipe is communicated with condensing crystallizing process tank.
As a kind of optimal technical scheme of the present utility model, one end of described condensing crystallizing process tank is provided with the 3rd delivery line,
One end of described 3rd delivery line is communicated with recovery ammonia storehouse.
As a kind of optimal technical scheme of the present utility model, in described filling storehouse, it is provided with oxidant.
As a kind of optimal technical scheme of the present utility model, at described extraction copper storehouse, described impurity and purification storehouse, described condensing crystallizing
Being provided with steady rest between reason tank and Su Suoshu recovery ammonia storehouse, the side of described steady rest is provided with some support columns, described
One end of dagger is provided with mounting seat.
The utility model is reached to provide the benefit that: treatment effeciency is high, improves the efficiency carrying out metal recovery；In filling storehouse
The oxidant of interior interpolation, can enter ammonia process by adding tube and process storehouse, heavy metal waste can be made to accomplish minimizing to greatest extent
With innoxious；Improve the efficiency of later stage process；Simple in construction, easy to use.
Accompanying drawing explanation
Accompanying drawing is used for providing being further appreciated by of the present utility model, and constitutes a part for specification, with of the present utility model
Embodiment is used for explaining the utility model together, is not intended that restriction of the present utility model.In the accompanying drawings:
Fig. 1 is structural representation of the present utility model；
In figure: 1, alkali leaching processes storehouse；2, the first communicating pipe；3, ammonia process processes storehouse；4, the second communicating pipe；5, extraction copper storehouse；
6, the first delivery line；7, impurity and purification storehouse；8, the second delivery line；9, condensing crystallizing process tank；10, the 3rd delivery line；
11, recovery ammonia storehouse；12, adding tube；13, filling storehouse；14, support column；15, steady rest；16, mounting seat.
Detailed description of the invention
Below in conjunction with accompanying drawing, preferred embodiment of the present utility model is illustrated, it will be appreciated that described herein be preferable to carry out
Example is merely to illustrate and explains the utility model, is not used to limit the utility model.
Embodiment
As it is shown in figure 1, the utility model provides a kind of cupric, nickel heavy metal waste utilization system, process storehouse including alkali leaching
1 and alkali leaching process storehouse 1 one end be provided with for the first communicating pipe 2, one end of the first communicating pipe 2 be communicated with ammonia process process storehouse 3 and
Ammonia process processes the one end in storehouse 3 and was provided with for the second communicating pipe 4, and one end of the second communicating pipe 4 is communicated with extraction copper storehouse 5.
Further, ammonia process processes the side in storehouse 3 and is provided with adding tube 12, and one end of adding tube 12 is provided with filling storehouse 13.
The one end in extraction copper storehouse 5 is provided with one end of the first delivery line 6 and the first delivery line 6 and is communicated with impurity and purification storehouse 7, removal of impurities
One end of cleaning position 7 is provided with one end of the second delivery line 8 and the second delivery line 8 and is communicated with condensing crystallizing process tank 9.
One end of condensing crystallizing process tank 9 is provided with the 3rd delivery line 10, and one end of the 3rd delivery line 10 is communicated with recovery ammonia storehouse
11。
It is provided with oxidant in filling storehouse 13.
It is provided with steady rest 15 between extraction copper storehouse 5, impurity and purification storehouse 7, condensing crystallizing process tank 9 and Soviet Union recovery ammonia storehouse 11,
The side of steady rest 15 is provided with some support columns 14, and one end of support column 14 is provided with mounting seat 16.
The utility model is using when, and heavy metal waste processes storehouse 1 through alkali leaching and carries recovery chromium, reclaims the alkali after chromium and carries
Slag processes in storehouse 3 with ammonia process leaching nickel, copper at ammonia process, ammonia leaching solution again through extraction copper, extract nickel, impurity and purification, condensing crystallizing,
After the leading process synthesis such as recovery ammonia utilizes, heavy metal waste can be made to accomplish minimizing to greatest extent and innoxious, and utilize back
The heavy metal received produces nickel sulfate, copper sulphate and sodium chromate product.
Treatment effeciency of the present utility model is high, improves the efficiency carrying out metal recovery；The oxidant added in filling storehouse 13,
Ammonia process can be entered by adding tube 12 and process storehouse 3, heavy metal waste can be made to accomplish minimizing to greatest extent and innoxious；Carry
The efficiency that the high later stage processes；Simple in construction, easy to use.
Last it is noted that the foregoing is only preferred embodiment of the present utility model, it is not limited to this practicality new
Type, although the utility model being described in detail with reference to previous embodiment, for a person skilled in the art, its
Still the technical scheme described in foregoing embodiments can be modified, or wherein portion of techniques feature is carried out equivalent replace
Change.All within spirit of the present utility model and principle, any modification, equivalent substitution and improvement etc. made, should be included in
Within protection domain of the present utility model.
Claims (6)
1. a cupric, nickel heavy metal waste utilization system, it is characterised in that include that alkali leaching processes storehouse (1) and institute
The one end stating alkali leaching process storehouse (1) is provided with the first communicating pipe (2), and one end of described first communicating pipe (2) is communicated with
Ammonia process processes one end of storehouse (3) and described ammonia process process storehouse (3) and is provided with the second communicating pipe (4), described second connection
One end of pipe (4) is communicated with extraction copper storehouse (5).
A kind of cupric, nickel heavy metal waste utilization system the most according to claim 1, it is characterised in that described
Ammonia process processes the side in storehouse (3) and is provided with adding tube (12), and one end of described adding tube (12) is provided with filling storehouse (13).
A kind of cupric, nickel heavy metal waste utilization system the most according to claim 1, it is characterised in that described
One end of extraction copper storehouse (5) is provided with one end of the first delivery line (6) and described first delivery line (6), and to be communicated with removal of impurities clean
Changing storehouse (7), one end of described impurity and purification storehouse (7) is provided with the second delivery line (8) and described second delivery line (8)
One end be communicated with condensing crystallizing process tank (9).
A kind of cupric, nickel heavy metal waste utilization system the most according to claim 3, it is characterised in that described
One end of condensing crystallizing process tank (9) is provided with the 3rd delivery line (10), and one end of described 3rd delivery line (10) is even
It is connected with recovery ammonia storehouse (11).
A kind of cupric, nickel heavy metal waste utilization system the most according to claim 2, it is characterised in that described
Filling storehouse is provided with oxidant in (13).
A kind of cupric, nickel heavy metal waste utilization system the most according to claim 4, it is characterised in that described
Extraction copper storehouse (5), described impurity and purification storehouse (7), described condensing crystallizing process tank (9) and Su Suoshu recovery ammonia storehouse (11)
Between be provided with steady rest (15), the side of described steady rest (15) is provided with some support columns (14), described
One end of dagger (14) is provided with mounting seat (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620075291.5U CN205528954U (en) | 2016-01-26 | 2016-01-26 | Copper -containing, nickel heavy metal comprehensive utilization of waste materials system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620075291.5U CN205528954U (en) | 2016-01-26 | 2016-01-26 | Copper -containing, nickel heavy metal comprehensive utilization of waste materials system |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205528954U true CN205528954U (en) | 2016-08-31 |
Family
ID=56769707
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620075291.5U Expired - Fee Related CN205528954U (en) | 2016-01-26 | 2016-01-26 | Copper -containing, nickel heavy metal comprehensive utilization of waste materials system |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205528954U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626716A (en) * | 2017-09-27 | 2018-01-26 | 新中天环保股份有限公司 | A kind of borate glass curing process |
-
2016
- 2016-01-26 CN CN201620075291.5U patent/CN205528954U/en not_active Expired - Fee Related
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN107626716A (en) * | 2017-09-27 | 2018-01-26 | 新中天环保股份有限公司 | A kind of borate glass curing process |
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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: 341600 Xingcun Avenue, Xinfeng County Industrial Park, Ganzhou City, Jiangxi Province Patentee after: Jiangxi Best Environmental Technology Co., Ltd. Address before: 341600 Xingcun Avenue, Xinfeng County Industrial Park, Ganzhou City, Jiangxi Province Patentee before: JIANGXI CHUANGHE CHONGSHENG ENVIRONMENT TECHNOLOGY CO., LTD. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20160831 Termination date: 20210126 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |