CN109208035A - Electrolysis production system and its construction method for magnesiothermy production titanium sponge - Google Patents

Electrolysis production system and its construction method for magnesiothermy production titanium sponge Download PDF

Info

Publication number
CN109208035A
CN109208035A CN201811238129.0A CN201811238129A CN109208035A CN 109208035 A CN109208035 A CN 109208035A CN 201811238129 A CN201811238129 A CN 201811238129A CN 109208035 A CN109208035 A CN 109208035A
Authority
CN
China
Prior art keywords
electrolysis
electrolyte
ingredient
magnesium
slot
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
Application number
CN201811238129.0A
Other languages
Chinese (zh)
Inventor
马尚润
朱福兴
李开华
苗庆东
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.)
Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
Original Assignee
Pangang Group Panzhihua Iron and Steel Research Institute 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
Publication date
Application filed by Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd filed Critical Pangang Group Panzhihua Iron and Steel Research Institute Co Ltd
Priority to CN201811238129.0A priority Critical patent/CN109208035A/en
Publication of CN109208035A publication Critical patent/CN109208035A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C3/00Electrolytic production, recovery or refining of metals by electrolysis of melts
    • C25C3/04Electrolytic production, recovery or refining of metals by electrolysis of melts of magnesium
    • CCHEMISTRY; METALLURGY
    • C22METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
    • C22BPRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
    • C22B34/00Obtaining refractory metals
    • C22B34/10Obtaining titanium, zirconium or hafnium
    • C22B34/12Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08
    • C22B34/1263Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction
    • C22B34/1268Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams
    • C22B34/1272Obtaining titanium or titanium compounds from ores or scrap by metallurgical processing; preparation of titanium compounds from other titanium compounds see C01G23/00 - C01G23/08 obtaining metallic titanium from titanium compounds, e.g. by reduction using alkali or alkaline-earth metals or amalgams reduction of titanium halides, e.g. Kroll process
    • CCHEMISTRY; METALLURGY
    • C25ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
    • C25CPROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
    • C25C7/00Constructional parts, or assemblies thereof, of cells; Servicing or operating of cells
    • C25C7/06Operating or servicing

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Electrochemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The invention discloses a kind of electrolysis production systems and its construction method for magnesiothermy production titanium sponge, belong to non-ferrous metal metallurgy production equipment and technology field.It is low to provide a kind of labor intensity, electrolysis effectiveness is good, the relatively long electrolysis production system and its construction method for magnesiothermy production titanium sponge of service life of equipment.The electrolysis production system includes electrolyte ingredient regulating device, electrolyte purification device, electrolysis of magnesium chloride device and ingredient separating device, the electrolyte ingredient regulating device, electrolyte purification device, electrolysis of magnesium chloride device and ingredient separating device sequential communication.The construction method refines the quality that slot is adjusted into the electrolyte in multipole slot by electrolyte ingredient regulating tank and anode upper plug type, then the magnesium chloride obtained is closed by the multipole electrolytic tank electrolysis constituent adjustment and obtains magnesium-electrolyte solution, separates magnesium from the magnesium-electrolyte solution finally by ingredient separating device.

Description

Electrolysis production system and its construction method for magnesiothermy production titanium sponge
Technical field
The present invention relates to a kind of electrolysis production systems, raw more particularly, to a kind of electrolysis for magnesiothermy production titanium sponge Production system belongs to non-ferrous metal metallurgy production equipment and technology field.It is given birth to the invention further relates to a kind of using the electrolysis The construction method of production system electrolysis production magnesium.
Background technique
Magnesium eletrolysis is that magnesiothermy production titanium sponge technique realizes magnesium-chlorine circulation core link.China's magnesium eletrolysis technology base Originally the various magnesium eletrolysis groove profile technologies in the world are covered, whether there is or not partition board electrolytic cell, assembly line electrolytic cell, multipole slots.Multipole slot is because of it Good economic indicator makes it achieve biggish market, the overall target and labor intensity of non-inductive windings electrolytic cell at home quickly It is high compared with multipolarity electrolytic cell, but it is relatively low to feed quality requirements, still there is least a portion of market.More non-inductive windings are electrolysed Slot, electrolyte ingredient regulating tank are connected with magnesium-electrolyte separating tank, form assembly line electrolytic cell, concentrate and realize magnesium-electrolyte point From, labor intensity is improved significantly, in addition, due to increasing electrolyte refining and constituent adjustment function, it is available The relatively poor raw material of material quality can especially match with large-scale " I " type furnace, it is made also to have city in magnesium eletrolysis technique ?.In order to further promote the competitiveness in magnesium eletrolysis technique of multipole slot for the mutual supplement with each other's advantages of multipole slot and flowing water wire casing And attraction, how to constitute a kind of pipeline system multipole slot and its application method just becomes those skilled in the art and is badly in need of solving The technical issues of.
Summary of the invention
The technical problems to be solved by the present invention are: providing, a kind of labor intensity is low, and electrolysis effectiveness is good, service life of equipment The relatively long electrolysis production system for magnesiothermy production titanium sponge.The present invention also provides one kind to give birth to for the electrolysis Produce the construction method of system.
Used technical solution is to solve above-mentioned technical problem: a kind of electrolysis for magnesiothermy production titanium sponge is raw Production system, the electrolysis production system include electrolyte ingredient regulating device, electrolyte purification device, electrolysis of magnesium chloride device And ingredient separating device, the electrolyte ingredient regulating device, electrolyte purification device, electrolysis of magnesium chloride device and ingredient Separator sequential communication.
Further, the electrolyte ingredient regulating device, electrolyte purification device, electrolysis of magnesium chloride device and Ingredient separating device passes through pulsometer and the melt canal sequential communication connecting with the pulsometer.
The preferred mode of the above solution is that the electrolyte ingredient regulating device is an electrolyte ingredient regulating tank.
Further, the electrolyte purification device is made of anode upper plug type refining slot.
The preferred mode of the above solution is that the anode upper plug type refining slot is to insert on anode described in two, two Formula refines slot and is serially connected between the electrolyte ingredient regulating device and the electrolysis of magnesium chloride device along flow direction of material.
Further, the electrolysis of magnesium chloride device is made of multipole slot.
The preferred mode of the above solution is that at least 3 groups of multipole slot of the electrolysis of magnesium chloride device are constituted, described in each group Multipole slot is linked in sequence along flow direction of material, and multipole slot described in first group is connected to the electrolyte purification device, described in last group Multipole slot be connected to the ingredient separating device.
Further, the multipole slot for constituting the electrolysis of magnesium chloride device is eight to ten groups.
Further, the ingredient separating device is made of magnesium-electrolyte separating tank.
A kind of construction method using the electrolysis production system electrolysis production titanium sponge, the construction method pass through institute The electrolyte ingredient regulating device and the electrolyte purification device stated are adjusted into the quality of the electrolyte in multipole slot, so Magnesium-electrolyte solution is obtained by the magnesium chloride that the electrolysis of magnesium chloride device is electrolysed constituent adjustment qualification afterwards, finally by Ingredient separating device separates magnesium from the magnesium-electrolyte solution.
The beneficial effects of the present invention are: the application is by by the existing electrolyte ingredient regulating device, electrolyte Purification device, electrolysis of magnesium chloride device and ingredient separating device sequential communication constitute the electrolysis production system.In this way, by It is provided with electrolyte ingredient regulating device and electrolyte purification device in the front end in production line, thus can be by quality phase Raw materials for production to poor raw material as the application electrolysis production system, simultaneously because impurity in electrolyte ingredient regulating tank and The refining slot sedimentation of anode upper plug type can also improve the service life of electrolytic cell;Correspondingly, due to increasing again in the end of production line If ingredient separating device, being automatically separated for electrolytic production may be implemented, and then can also greatly reduce the labour of operator Intensity.
Detailed description of the invention
Fig. 1 is the simplified structure diagram for the electrolysis production system that the present invention produces titanium sponge for magnesiothermy.
In the figure, it is marked as electrolyte ingredient regulating device 1, electrolyte purification device 2, electrolysis of magnesium chloride device 3, ingredient point From device 4, melt canal 5.
Specific embodiment
It is that a kind of labor intensity provided by the invention is low as shown in Figure 1, electrolysis effectiveness is good, and service life of equipment is relatively long For magnesiothermy production titanium sponge electrolysis production system and a kind of construction method for the electrolysis production system.Institute The electrolysis production system stated includes electrolyte ingredient regulating device 1, electrolyte purification device 2, electrolysis of magnesium chloride device 3 and ingredient Separator 4, the electrolyte ingredient regulating device 1, electrolyte purification device 2, electrolysis of magnesium chloride device 3 and ingredient point From 4 sequential communication of device.The construction method passes through the electrolyte ingredient regulating device 1 and the electrolyte purification Device 2 is adjusted into the quality of the electrolyte in multipole slot, is then electrolysed constituent adjustment by the electrolysis of magnesium chloride device 3 It closes the magnesium chloride that obtains and obtains magnesium-electrolyte solution, finally by ingredient separating device 4 by magnesium from the magnesium-electrolyte solution In separate.The application is by by the existing electrolyte ingredient regulating device 1, electrolyte purification device 2, magnesium chloride Electrolysis unit 3 and 4 sequential communication of ingredient separating device constitute the electrolysis production system.In this way, due in production line Front end is provided with electrolyte ingredient regulating device 1 and electrolyte purification device 2, thus original that can be relatively poor by quality The raw materials for production as the application electrolysis production system are expected, simultaneously because impurity is in electrolyte ingredient regulating tank and anode upper plug type Refining slot sedimentation can also improve the service life of electrolytic cell;Correspondingly, due to adding ingredient separation again in the end of production line Device 4 may be implemented being automatically separated for electrolytic production, and then can also greatly reduce the labor intensity of operator.At this point, The electrolyte ingredient regulating device 1, electrolyte purification device 2, electrolysis of magnesium chloride device 3 and ingredient separating device 4 are excellent It is selected as through 5 sequential communication of pulsometer and the melt canal being connect with the pulsometer.Correspondingly, pulsometer of the present invention is excellent First using the pulsometer in utility model " a kind of pulsometer (ZL 2,016 2 0042695.4) for conveying high-temperature molten salt ".
In above embodiment, in order in conjunction with existing U.S. electrolysis installation, realize the logical of equipment component as far as possible With change and standard, the electrolyte ingredient regulating device 1 is an electrolyte ingredient regulating tank.The electrolyte purification dress 2 are set to be made of anode upper plug type refining slot.The electrolysis of magnesium chloride device 3 is made of multipole slot.The ingredient separates dress 4 are set to be made of magnesium-electrolyte separating tank.Correspondingly, in order to improve the depuration quality of electrolyte, the anode upper plug type refining Slot is that the refining slot of anode upper plug type described in two, two is serially connected in the electrolyte ingredient regulating tank and head along flow direction of material Between a multipole slot.In order to improve the electrolysis production efficiency of whole system, the more of the electrolysis of magnesium chloride device 3 are constituted At least 3 groups of pole slot, multipole slot described in each group is linked in sequence along flow direction of material, multipole slot described in first group and the electrolyte Purification device 2 is connected to, and the group multipole slot in end is connected to the ingredient separating device 4.This preferred embodiment is, described in composition The multipole slot of electrolysis of magnesium chloride device 3 is eight to ten groups.
In conclusion using electrolysis production system provided by the present application under electrolysis construction method provided by the present application guidance Magnesium eletrolysis production is carried out to have further the advantage that,
The labor intensity of multipole slot can be reduced by concentrating charging and taking out magnesium;By in electrolyte ingredient regulating tank and anode Upper plug type refining slot, which carries out purification to electrolyte, can be used low-quality raw material;Impurity is on electrolyte ingredient regulating tank and anode The service life of electrolytic cell can be improved in the formula of inserting refining slot sedimentation.Multipole slot technology is promoted in the influence power and competition of industry with this Power.
The explanation under is carried out to electrolysis production system and electrolysis production construction method of the invention below by embodiment.
Embodiment 1:
Certain titanium sponge factory uses multipole slot technology, and device is multipole slot.The application method of multipole slot is carried out in single slot Magnesium is taken out in charging, and no purifying electrolysis slot can not carry out removing slag operation.Using the technology, current efficiency 80%, ton magnesium direct current Consumption is 11500kWh;Since single slot feeds and take out magnesium, the ton magnesium cost of labor of multipole slot is 953 yuan;Since multipole slot does not have Purification function, raw material MgCl2Content requirement be not less than 99.95%, content of MgO is of less demanding in 0.1% in raw material;Due to more Pole slot is in whole sealing status, can not remove the gred to electrolytic cell, and electrolytic cell service life is 24 months.
Embodiment 2:
Certain titanium sponge factory uses pipeline system magnesium eletrolysis technology, and device mainly includes: electrolyte ingredient regulating tank, anode Upper plug type refines slot, anode down inserting type flowing water wire casing, magnesium-electrolyte separating tank and melt canal.Assembly line magnesium eletrolysis technology Application method is by multipole slot and the electrolyte ingredient regulating tank of pipeline system magnesium eletrolysis, anode upper plug type refining slot and magnesium- Electrolyte separating tank is connected using melt canal, realizes Matter Transfer by pulsometer.Using the technology, current efficiency is 78%, ton magnesium direct current consumption is 13670kWh;By concentrating charging and taking out magnesium, ton magnesium cost of labor is 523 yuan;By being electrolysed Matter constituent adjustment slot and anode upper plug type refining slot purify raw material, and MgCl can be used2Content is that 95% or more, MgO contains Amount is in 0.5% raw material below;It is removed the gred by refining slot in electrolyte ingredient regulating tank and anode upper plug type, electrolytic cell Service life can be improved to 40 months;Multipole slot technology is promoted in the influence power and competitiveness of industry.
Embodiment 3:
Using pipeline system multipole slot technology of the present invention, device mainly includes: multipole slot, electrolyte ingredient regulating tank, Anode upper plug type refines slot, magnesium-electrolyte separating tank and melt canal.The application method of pipeline system multipole slot technology is will be more Pole slot and the electrolyte ingredient regulating tank of pipeline system magnesium eletrolysis, anode upper plug type refining slot and magnesium-electrolyte separating tank are adopted It is connected with melt canal, Matter Transfer is realized by pulsometer.Using the technology, current efficiency 79%, ton magnesium direct current Power consumption is 11670kWh;By concentrating charging and taking out magnesium, ton magnesium cost of labor is 463 yuan;By in electrolyte ingredient regulating tank Raw material is purified with anode upper plug type refining slot, MgCl can be used2Content is 95% or more, and content of MgO is below 0.5% Raw material;It is removed the gred by refining slot in electrolyte ingredient regulating tank and anode upper plug type, the service life of electrolytic cell can mention Up to 40 months.

Claims (10)

1. a kind of electrolysis production system for magnesiothermy production titanium sponge, it is characterised in that: the electrolysis production system packet Electrolyte ingredient regulating device (1), electrolyte purification device (2), electrolysis of magnesium chloride device (3) and ingredient separating device (4) are included, Electrolyte ingredient regulating device (1), electrolyte purification device (2), electrolysis of magnesium chloride device (3) and the ingredient separation dress Set (4) sequential communication.
2. the electrolysis production system according to claim 1 for magnesiothermy production titanium sponge, it is characterised in that: described Electrolyte ingredient regulating device (1), electrolyte purification device (2), electrolysis of magnesium chloride device (3) and ingredient separating device (4) Pass through pulsometer and the melt canal connecting with the pulsometer (5) sequential communication.
3. the electrolysis production system according to claim 1 or 2 for magnesiothermy production titanium sponge, it is characterised in that: institute The electrolyte ingredient regulating device (1) stated is an electrolyte ingredient regulating tank.
4. the electrolysis production system according to claim 1 or 2 for magnesiothermy production titanium sponge, it is characterised in that: institute The electrolyte purification device (2) stated is made of anode upper plug type refining slot.
5. the electrolysis production system according to claim 4 for magnesiothermy production titanium sponge, it is characterised in that: described Anode upper plug type refining slot is that the refining slot of anode upper plug type described in two, two is serially connected in the electrolyte along flow direction of material Between component adjusting device (1) and the electrolysis of magnesium chloride device (3).
6. the electrolysis production system according to claim 1 or 2 for magnesiothermy production titanium sponge, it is characterised in that: institute The electrolysis of magnesium chloride device (3) stated is made of multipole slot.
7. the electrolysis production system according to claim 6 for magnesiothermy production titanium sponge, it is characterised in that: constitute institute At least 3 groups of multipole slot for stating electrolysis of magnesium chloride device (3), multipole slot described in each group are linked in sequence along flow direction of material, first group of institute The multipole slot stated is connected to the electrolyte purification device (2), the end group multipole slot and the ingredient separating device (4) it is connected to.
8. the electrolysis production system according to claim 6 for magnesiothermy production titanium sponge, it is characterised in that: constitute institute The multipole slot for stating electrolysis of magnesium chloride device (3) is eight to ten groups.
9. the electrolysis production system according to claim 1 or 2 for magnesiothermy production titanium sponge, it is characterised in that: institute The ingredient separating device (4) stated is made of magnesium-electrolyte separating tank.
10. a kind of construction method using electrolysis production system electrolysis production titanium sponge described in claim 1, it is characterised in that: The construction method by the electrolyte ingredient regulating device (1) and the electrolyte purification device (2) adjust into Enter the quality of the electrolyte in multipole slot, the chlorine of constituent adjustment qualification is then electrolysed by the electrolysis of magnesium chloride device (3) Change magnesium and obtain magnesium-electrolyte solution, separates magnesium from the magnesium-electrolyte solution finally by ingredient separating device (4) Out.
CN201811238129.0A 2018-10-23 2018-10-23 Electrolysis production system and its construction method for magnesiothermy production titanium sponge Pending CN109208035A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811238129.0A CN109208035A (en) 2018-10-23 2018-10-23 Electrolysis production system and its construction method for magnesiothermy production titanium sponge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811238129.0A CN109208035A (en) 2018-10-23 2018-10-23 Electrolysis production system and its construction method for magnesiothermy production titanium sponge

Publications (1)

Publication Number Publication Date
CN109208035A true CN109208035A (en) 2019-01-15

Family

ID=64981426

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811238129.0A Pending CN109208035A (en) 2018-10-23 2018-10-23 Electrolysis production system and its construction method for magnesiothermy production titanium sponge

Country Status (1)

Country Link
CN (1) CN109208035A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114317966A (en) * 2022-01-14 2022-04-12 新疆湘晟新材料科技有限公司 Arrangement method of reduction distillation device and magnesium electrolytic cell device for titanium sponge production

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1210817A (en) * 1997-05-23 1999-03-17 朴荣培 Multipolar-type electrolytic bath and apparatus for purifying waste and contaminated water using the same
CN203247315U (en) * 2013-04-21 2013-10-23 武汉兴达高技术工程有限公司 Bipolar electrolysis bath
CN106283114A (en) * 2016-09-05 2017-01-04 攀钢集团攀枝花钢铁研究院有限公司 For extending control method and the graphite electrode thereof in graphite electrode service life
CN107236968A (en) * 2017-08-09 2017-10-10 攀钢集团研究院有限公司 A kind of and supporting magnesium eletrolysis method of large-scale I types stove

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1210817A (en) * 1997-05-23 1999-03-17 朴荣培 Multipolar-type electrolytic bath and apparatus for purifying waste and contaminated water using the same
CN203247315U (en) * 2013-04-21 2013-10-23 武汉兴达高技术工程有限公司 Bipolar electrolysis bath
CN106283114A (en) * 2016-09-05 2017-01-04 攀钢集团攀枝花钢铁研究院有限公司 For extending control method and the graphite electrode thereof in graphite electrode service life
CN107236968A (en) * 2017-08-09 2017-10-10 攀钢集团研究院有限公司 A kind of and supporting magnesium eletrolysis method of large-scale I types stove

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
姜宝伟等: "海绵钛生产工艺中几种镁电解槽技术的对比分析", 《轻金属》 *

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN114317966A (en) * 2022-01-14 2022-04-12 新疆湘晟新材料科技有限公司 Arrangement method of reduction distillation device and magnesium electrolytic cell device for titanium sponge production
CN114317966B (en) * 2022-01-14 2023-08-18 新疆湘晟新材料科技有限公司 Arrangement method of reduction distillation device and magnesium electrolytic tank device for producing titanium sponge

Similar Documents

Publication Publication Date Title
CN103740945B (en) A kind of method of enriching and recovering cadmium from plumbous smelting system
CN102648298B (en) Method for removal of chloride from zinc sulphate solution
CN104220646A (en) System for power control in cells for electrolytic recovery of a metal
CN106756024A (en) A kind of method of cobalt impurity in purifying zinc sulfate solution
CN106048659A (en) Spent solution treatment method of silver electrolyte
CN109208035A (en) Electrolysis production system and its construction method for magnesiothermy production titanium sponge
CN106086461A (en) A kind of method of Copper making process slag making arsenic removal
CN109763140A (en) A kind of preparation method of the ultrapure copper of 7N
CN104805468A (en) Process for preparing zinc by using zinc oxide material containing complex components like Cu, Pb, Zn, and Ag
CN106164305A (en) The manufacture method of tough cathode
CN103695961A (en) Method for recovering rhenium, arsenic and copper from sulfuric acid wastewater of copper smelting flue gas purification system
CN105350020A (en) Aluminum electrolysis cell provided with continuous anode
CN208250436U (en) It is electrolysed copper scap anode frame
CN1673418A (en) Production of aluminium by low-temperature electrolytic process and special aluminium electrolytic tank thereof
CN104005051A (en) Method for extracting electrodeposited zinc from zinc oxide powder in ammonium chloride solution system
CN207091520U (en) A kind of turbulent flow electrowinning plant for being used to handle waste silver electrolyte
CN104746106B (en) Molten salt electrolysis method for preparing aluminum-scandium intermediate alloy
WO2016114439A1 (en) Method for simultaneously recovering cobalt and manganese from lithium based battery
CN102268692B (en) Method for producing cathode copper by directly electrolyzing spongy copper
CN106835196A (en) Produce the mixing electrolysis system of tough cathode
CN108149020B (en) The technique for preparing bismuth using zinc anode sludge waste residue
CN102492960A (en) Method for preparing cathode copper by high-nickel content copper plate as anode
CN105821443A (en) Production process of cathode copper
CN102234816A (en) Method for extracting copper from copper electrolyte
CN102864313A (en) Smelting method of natural copper mine

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
RJ01 Rejection of invention patent application after publication

Application publication date: 20190115

RJ01 Rejection of invention patent application after publication