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 PDF

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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
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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
Application number
CN201620075291.5U
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Chinese (zh)
Inventor
邓才宇
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangxi Best Environmental Technology Co., Ltd.
Original Assignee
Jiangxi Chuanghe Chongsheng Environment Technology Co ltd
Priority date (The priority date 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 date listed.)
Filing date
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Priority to CN201620075291.5U priority Critical patent/CN205528954U/en
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Publication of CN205528954U publication Critical patent/CN205528954U/en
Expired - Fee Related legal-status Critical Current
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/20Recycling

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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

A kind of cupric, nickel heavy metal waste utilization system
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).
CN201620075291.5U 2016-01-26 2016-01-26 Copper -containing, nickel heavy metal comprehensive utilization of waste materials system Expired - Fee Related CN205528954U (en)

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

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CN205528954U true CN205528954U (en) 2016-08-31

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Cited By (1)

* Cited by examiner, † Cited by third party
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

Cited By (1)

* Cited by examiner, † Cited by third party
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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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