CN109295479A - The rotating flow electrowinning plant of heavy metal in a kind of recycling slag - Google Patents
The rotating flow electrowinning plant of heavy metal in a kind of recycling slag Download PDFInfo
- Publication number
- CN109295479A CN109295479A CN201811220480.7A CN201811220480A CN109295479A CN 109295479 A CN109295479 A CN 109295479A CN 201811220480 A CN201811220480 A CN 201811220480A CN 109295479 A CN109295479 A CN 109295479A
- Authority
- CN
- China
- Prior art keywords
- heavy metal
- cathode
- slag
- rotating flow
- anode
- 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.)
- Pending
Links
- 229910001385 heavy metal Inorganic materials 0.000 title claims abstract description 23
- 239000002893 slag Substances 0.000 title claims abstract description 17
- 238000005363 electrowinning Methods 0.000 title claims abstract description 11
- 238000004064 recycling Methods 0.000 title abstract description 6
- 238000011084 recovery Methods 0.000 claims abstract description 12
- 239000003792 electrolyte Substances 0.000 claims abstract description 5
- 229910052751 metal Inorganic materials 0.000 claims abstract description 5
- 239000002184 metal Substances 0.000 claims abstract description 5
- 239000000843 powder Substances 0.000 claims description 3
- 230000001376 precipitating effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 6
- KHYBPSFKEHXSLX-UHFFFAOYSA-N iminotitanium Chemical compound [Ti]=N KHYBPSFKEHXSLX-UHFFFAOYSA-N 0.000 abstract description 5
- 229910001000 nickel titanium Inorganic materials 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000243 solution Substances 0.000 description 9
- 238000004070 electrodeposition Methods 0.000 description 6
- 239000007788 liquid Substances 0.000 description 3
- 239000002253 acid Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000005864 Sulphur Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000004090 dissolution Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 239000006166 lysate Substances 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 150000002739 metals Chemical class 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C7/00—Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C1/00—Electrolytic production, recovery or refining of metals by electrolysis of solutions
Abstract
The invention belongs to abandoned mine metal in the dreg field of resource recovery technique more particularly to a kind of for recycling the rotating flow electrowinning plant of heavy metal in slag.Device includes cylindrical metallic cathode plate, square column Ni―Ti anode, tubular plastic shell.Metallic cathode plate is axially corrugation face straight tube shape.Electrolyte is entered by bottom of device, by flowing out at the top of device.Cathode can deposit heavy metal.Device technique provided by the invention is simple, reliable for operation, increases the contact area of electrolyte and cathode.Heavy metal recovery field has the advantages that the rate of recovery is high, product purity is high, production cost is low etc. in slag.
Description
Technical field
The invention belongs to heavy metal resources utilization technology fields in abandoned mine slag, are related to a kind of for handling the rotation of slag
Turn of tidal stream electrowinning plant.
Technical background
Heavy metal containing 1000ppm or more in the certain dump slags generated after ore smelting, these heavy metals can
To carry out recycling and reusing.After actual technique generally uses the heavy metal in acid dissolution slag, recycled using the method for electrodeposition.
But general Winning cell is to put one or more pairs of anode and cathode metal plates in rectangular pond to carry out energization recycling.Because electrolyte cannot fill
It point is contacted with cathode plate, leads to that the not high heavy metal recovery rate of this Winning cell, metals content impurity height of recycling, energy consumption is high
Problem.In addition also there is cartridge type turbulent flow electrodeposition equipment at present, improve the rate of recovery of heavy metal, but still not ideal enough.Therefore make
Electrolyte is sufficiently and cathode contacts, the rate of recovery for increasing heavy metal are very necessary.
Summary of the invention
The rotating flow for being preferably used to handle heavy metal recovery in slag the purpose of the invention is to provide a kind of effect
Electrowinning plant specifically adopts the following technical scheme that:
It is a kind of for handling the rotating flow electrowinning plant of slag, which is characterized in that include rotating flow Winning cell, cathode tube
Heavy metal powder can be precipitated in body, cathode;Anode is located in the middle part of cathode cylinder, and anode uses square column Ni―Ti anode, cathode tube
It include solution inlet port below body, top includes taphole.
The further technical solution of the present invention is, can make multiple electrodeposition equipment in parallel or series, can advanced treating containing a huge sum of money
Belong to solution.
It using the present invention of technical solution as above, has the advantages that compared with the existing technology: increasing solution and yin
The contact of pole improves the rate of recovery of heavy metal.Easy to operate, maintenance cost is low.Modularization is readily transported.
Detailed description of the invention
In order to further illustrate the present invention, it is illustrated with reference to the accompanying drawing:
Fig. 1 is the standby structural schematic diagram that rotating flow electrodeposition of the invention is set, including 1. plastic shells;2. inlet;3. going out
Liquid mouth;4. cylinder cathode;5. square column Ni―Ti anode.
Fig. 2 is rotating flow Winning cell electrodeposition appearance schematic diagram of the present invention, including 1. square column Ni―Ti anodes;2. cartridge type is negative
Pole;3. cylinder cathode top view.
Specific embodiment
The embodiment of the present invention is illustrated with reference to the accompanying drawing, embodiment is not construed as limiting the invention:
A kind of rotating flow electrowinning plant for heavy metal recovery in slag, which is characterized in that it include rotating flow Winning cell,
Heavy metal powder can be precipitated in cathode cylinder, cathode;Anode is located in the middle part of cathode cylinder, and anode uses square column Ni―Ti anode,
It include solution inlet port below cathode cylinder, top includes taphole;It is connected between solution inlet port and taphole by pipeline
Winning cell.The technical effect and its realization process for the essence that the technical program is played are as follows: 30% sulphur is injected in slag
Acid dissolves the Leaching of Heavy Metals in slag, leaches solid-to-liquid ratio 1: 3~1: 10,1~6h of extraction time, extraction temperature 10~50
DEG C, and be stirred, heavy metal ion is contained in solution.Liquid exports to filter, filters particles in solution, into rotating flow
Electrowinning plant electrodeposition.100~1000A/m of current density2, electric effusion concentration of heavy metal ion≤10mg/L after processing, and return
Into technique front end injection lysate.It is dry after remaining slag discharge, it is discharged according to environmental requirement, or for building
Material production.
Claims (3)
1. a kind of rotating flow electrowinning plant for heavy metal recovery in slag, which is characterized in that include rotating flow Winning cell, rotation
Turn of tidal stream Winning cell includes cathode cylinder, and cylinder inboard wall has valley of corrugation axially, for increasing electrolyte and cathode cylinder
Contact area.Cathode connection column is welded with inner wall, and cathode can be with precipitating metal powder;Anode is located in the middle part of cathode cylinder, anode
For square-column-shaped stud, cathode cylinder lower section includes solution inlet port, and top includes taphole.
2. as described in claim 1 a kind of for handling the heavy metal recovery rotating flow electrowinning plant of slag, which is characterized in that
Cathodic metal cylinder plate has the valley of corrugation rectangular along axis.
3. as described in claim 1 a kind of for handling the heavy metal recovery rotating flow electrowinning plant of slag, which is characterized in that
Anode is square column stud.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811220480.7A CN109295479A (en) | 2018-10-12 | 2018-10-12 | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201811220480.7A CN109295479A (en) | 2018-10-12 | 2018-10-12 | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag |
Publications (1)
Publication Number | Publication Date |
---|---|
CN109295479A true CN109295479A (en) | 2019-02-01 |
Family
ID=65157282
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201811220480.7A Pending CN109295479A (en) | 2018-10-12 | 2018-10-12 | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN109295479A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110042426A (en) * | 2019-06-06 | 2019-07-23 | 深圳市中金岭南有色金属股份有限公司丹霞冶炼厂 | A kind of closed electrodeposition pipe and gallium electrodeposition system |
Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008004486A (en) * | 2006-06-26 | 2008-01-10 | Toyota Motor Corp | Manufacturing method of electrolyte film for fuel cell, and membrane electrode assembly |
CN103700507A (en) * | 2013-12-25 | 2014-04-02 | 佛山市高明区利明电子有限公司 | 100V electrolytic capacitor and producing process thereof |
KR20150116637A (en) * | 2014-04-08 | 2015-10-16 | 홍기섭 | Electrolyzer for withdrawing valuable metal |
CN204991852U (en) * | 2015-09-29 | 2016-01-20 | 张学麟 | Novel battery structure |
CN205529064U (en) * | 2016-01-29 | 2016-08-31 | 江苏净拓环保科技有限公司 | Copper device is retrieved in acid etching solution regeneration |
CN205974692U (en) * | 2016-07-11 | 2017-02-22 | 陕西瑞凯环保科技有限公司 | A torrent electrodeposition device for handling copper ashes |
CN107075701A (en) * | 2015-07-03 | 2017-08-18 | 阿库亚爱克斯公司 | Electrolysis unit and electrolysis ozone water making device |
CN209082012U (en) * | 2018-10-12 | 2019-07-09 | 浙江田成环境科技有限公司 | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag |
-
2018
- 2018-10-12 CN CN201811220480.7A patent/CN109295479A/en active Pending
Patent Citations (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2008004486A (en) * | 2006-06-26 | 2008-01-10 | Toyota Motor Corp | Manufacturing method of electrolyte film for fuel cell, and membrane electrode assembly |
CN103700507A (en) * | 2013-12-25 | 2014-04-02 | 佛山市高明区利明电子有限公司 | 100V electrolytic capacitor and producing process thereof |
KR20150116637A (en) * | 2014-04-08 | 2015-10-16 | 홍기섭 | Electrolyzer for withdrawing valuable metal |
CN107075701A (en) * | 2015-07-03 | 2017-08-18 | 阿库亚爱克斯公司 | Electrolysis unit and electrolysis ozone water making device |
CN204991852U (en) * | 2015-09-29 | 2016-01-20 | 张学麟 | Novel battery structure |
CN205529064U (en) * | 2016-01-29 | 2016-08-31 | 江苏净拓环保科技有限公司 | Copper device is retrieved in acid etching solution regeneration |
CN205974692U (en) * | 2016-07-11 | 2017-02-22 | 陕西瑞凯环保科技有限公司 | A torrent electrodeposition device for handling copper ashes |
CN209082012U (en) * | 2018-10-12 | 2019-07-09 | 浙江田成环境科技有限公司 | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110042426A (en) * | 2019-06-06 | 2019-07-23 | 深圳市中金岭南有色金属股份有限公司丹霞冶炼厂 | A kind of closed electrodeposition pipe and gallium electrodeposition system |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU651439B2 (en) | Mineral recovery apparatus | |
CN104831064B (en) | Acidleach-cyclone electrolytic cell technology technique of high efficiente callback copper from lead copper matte is pressed with oxygen | |
CN102534656B (en) | Process for recycling copper through electrodeposition by treating scrap copper materials by adopting cyclone electrolysis technology | |
CN107742760A (en) | Method for extracting lithium from waste lithium ion battery | |
CN102808194A (en) | Process for purifying cobalt by electro-depositing cobalt chloride solution through cyclone electrolysis technology and reclaiming residual chlorine | |
CN104451784A (en) | Rotational flow electrolyzing device for separating and recycling metal composite waste material | |
CN103320613A (en) | Method for recovering cobalt nickel through electrolytic manganese industrial ion exchange method | |
CN103668322B (en) | A kind of steamalloy waste recovery copper, the method for nickel | |
CN104404262A (en) | Copper scum treatment technique | |
CN109485023A (en) | A method of recycling tellurium from cupric tellurium waste liquid | |
CN209082012U (en) | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag | |
CN102268692B (en) | Method for producing cathode copper by directly electrolyzing spongy copper | |
CN105887118B (en) | A kind of method that Selective Separation from materials containing tellurium reclaims tellurium | |
CN106282569A (en) | A kind of copper-cadmium slag puies forward the method for cadmium residue resource reclaim | |
CN109295479A (en) | The rotating flow electrowinning plant of heavy metal in a kind of recycling slag | |
CN109536715A (en) | A kind of zinc lixiviating solution Cobalt Purification method | |
CN101545115A (en) | Method for producing electrolytic zinc from zinc oxide-containing materials | |
CN106893859B (en) | A method of processing nickel cobalt waste material | |
CN103060842A (en) | Method for preparing electrodeposited cobalt under large flow | |
CN206219686U (en) | A kind of alkaline etching liquid electrolysis carries copper system system | |
CN101250718A (en) | Method for electrodeposition of metallic nickel with nickel sulfide | |
CN102296325A (en) | Process for treating waste lead accumulator through continuous solid phase electrolysis of rotating cathode | |
CN104928476B (en) | A kind of processing method of cobalt-copper alloy Water Quenching Slag | |
CN107268029B (en) | The method and apparatus that a kind of waterpower unloads the lead solution continuous electrolysis of lead | |
CN204529999U (en) | A kind of swirl electrolysis device of Separation and Recovery metal composite waste |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
DD01 | Delivery of document by public notice |
Addressee: ZHEJIANG TIANCHENG ENVIRONMENT TECHNOLOGY CO.,LTD. Person in charge of patents Document name: Notice of First Examination Opinion |
|
DD01 | Delivery of document by public notice |