CN104775135A - Electrolysis bath alumina discharge control method - Google Patents

Electrolysis bath alumina discharge control method Download PDF

Info

Publication number
CN104775135A
CN104775135A CN201410014685.5A CN201410014685A CN104775135A CN 104775135 A CN104775135 A CN 104775135A CN 201410014685 A CN201410014685 A CN 201410014685A CN 104775135 A CN104775135 A CN 104775135A
Authority
CN
China
Prior art keywords
material discharge
housing
beating
breaking
crust
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
CN201410014685.5A
Other languages
Chinese (zh)
Inventor
李南谊
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.)
Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
Original Assignee
Guiyang Aluminum Magnesium Design and 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 Guiyang Aluminum Magnesium Design and Research Institute Co Ltd filed Critical Guiyang Aluminum Magnesium Design and Research Institute Co Ltd
Priority to CN201410014685.5A priority Critical patent/CN104775135A/en
Publication of CN104775135A publication Critical patent/CN104775135A/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
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/20Automatic control or regulation of cells
    • 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
    • C25C3/06Electrolytic production, recovery or refining of metals by electrolysis of melts of aluminium
    • C25C3/14Devices for feeding or crust breaking

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Electrochemistry (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Electrolytic Production Of Metals (AREA)

Abstract

The present invention discloses an electrolysis bath alumina discharge control method. According to the method, 6 groups of beating devices (1) and the gas cylinders on material discharge devices (2) are connected with 3 electromagnetic valves (3) respectively through a compressed air pipeline network (4), and the electromagnetic valve (3) controls the beating device (1) connected with the electromagnetic valve so as to achieve the two-device alternating material discharge, wherein the housing beating material discharge points 1 and 4, the housing beating material discharge points 2 and 5, and the housing beating material discharge points 3 and 6 are respectively controlled, or the housing beating material discharge points 1 and 6, the housing beating material discharge points 2 and 5, and the housing beating material discharge points 3 and 4 are respectively controlled, or the housing beating material discharge points 1 and 3, the housing beating material discharge points 2 and 4, and the housing beating material discharge points 5 and 6 are respectively controlled. According to the present invention, the three-device alternating material discharge in the traditional electrolysis bath alumina housing beating material discharge control technology is changed into the two-device alternating material discharge, such that the alumina is easily dissolved in the relatively high stability electrolysis bath so as to reduce the generation of the alumina precipitation and reduce the electric energy consumption.

Description

Electrolyzer alumina blanking control method
Technical field
The present invention relates to a kind of control method of electrolyzer alumina blanking.
Background technology
Modern aluminum industry is produced, and mainly take sodium aluminum fluoride-alumina molten salt electrolysis method to produce electrolytic aluminum, the raw material of that is electrolysis is aluminum oxide.Specific implementation process is: the equipment of electrolysis is electrolyzer, electrolyzer is configured with multiple alumina blanking point, each blanking point is configured with 1 and hits tup, aluminum oxide is added into blanking point by the blanking device be arranged in hopper, finally enter in electrolyzer fused solution and carry out electrolysis production, thus electrolysis goes out metal aluminium liquid.In whole implementation process, first aluminum oxide is rapid solution, is then slow dissolving.Slow dissolving is caused by condensing electrolyte effect.
Along with the development of aluminum i ndustry, cell capacity continues to increase, and therefore the length and width of electrolyzer also continue to increase thereupon, and the bath of cell minute surface namely maximized is larger.Simultaneously, in order to better deepen " energy-saving and emission-reduction " thought, reduce power consumption, current most electrolyzer all have employed the design of higher stability, and this kind of design is to reduce metal wave, reduce pole span, but also reduce the mobility of aluminium liquid simultaneously, finally cause electrolyte flow to reduce, thus, the aluminum oxide velocity of diffusion dropped in electrolyzer molten mass can reduce, thus produces condensation effects.
Current large prebaked cell for aluminum-reduction alumina feeding control techniques generally adopts the constant-volume blanking device 6 of 1.8L, three or three staggered blanking, i.e. blankings 5.4 kilograms.Because discharge quantity is larger, electrolyzer (particularly adopts special-shaped cathode and reduces horizontal current technology) after have employed the design of higher stability, reduce the mobility of aluminium liquid, finally cause electrolyte flow to reduce and easily in electrolyzer, produce precipitation, thus worsen the distribution of current of bath of cell, add the energy expenditure of electrolyzer.
Summary of the invention
The object of the invention is to: provide one can use in the design of electrolyzer high stability, the electrolyzer alumina blanking control method that can use on Large Copacity electrolyzer again, the electrolyte flow existed to overcome prior art reduces easily generation precipitation in electrolyzer, thus worsen the distribution of current of bath of cell, increase the deficiencies such as the energy expenditure of electrolyzer.
The present invention is formed like this: 6 groups of percussion devices are connected with 3 magnetic valves respectively by compressed air pipe network with the cylinder on blanking device, the percussion device be attached thereto by solenoid control realizes two or two staggered blankings, namely crust-breaking & baiting point 1 and 4, crust-breaking & baiting point 2 and 5, crust-breaking & baiting point 3 and 6 is controlled respectively, or control crust-breaking & baiting point 1 and 6, crust-breaking & baiting point 2 and 5, crust-breaking & baiting point 3 and 4 respectively, or control crust-breaking & baiting point 1 and 3, crust-breaking & baiting point 2 and 4, crust-breaking & baiting point 5 and 6 respectively.
The present invention is by traditional large scale electrolytic cell aluminum oxide crust-breaking & baiting control techniques, three or three staggered blankings change two or two staggered blankings into, namely alumina feeding adopts the constant-volume blanking device 6 of 1.8L, two or two staggered blankings, an i.e. blanking 3.6 kilograms thus decrease the discharge quantity of each blanking, aluminum oxide is easier to dissolve in the electrolyzer of higher stability, reduces the generation of precipitation of alumina, reduces the consumption of electric energy.
Accompanying drawing explanation
Fig. 1 is traditional electrolyte groove alumina blanking point control method schematic diagram;
Fig. 2 is electrolyzer alumina blanking point control method schematic diagram of the present invention.
Embodiment
Embodiments of the invention: the present invention is made up of percussion device 1, blanking device 2, magnetic valve 3, compressed air pipe network 4 etc., by compressed air pipe network 4 by 3 magnetic valves 3 with connect with the cylinders on 6 groups of percussion devices 1, blanking device 2 respectively, the percussion device 1 controlling to be attached thereto eventually through magnetic valve 3 realizes running, thus realizes two or two staggered blankings.
Range of application: as providing one can use in the design of electrolyzer high stability on the electrolyzer that this invention can be used in differing capacities, the control method of the electrolyzer alumina blanking that can use on Large Copacity electrolyzer again.The particular location of percussion device 1, blanking device 2, magnetic valve 3, compressed air pipe network 4 can adjust, and combination adjustment can be carried out, as (1-4 according to practical situation in two or two reference mark interlocked, 2-5,3-6 control), (1-6,2-5,3-4 controls), (1-3,2-4,5-6 control) etc.

Claims (1)

1. an electrolyzer alumina blanking control method, it is characterized in that: 6 groups of percussion devices (1) are connected with 3 magnetic valves (3) respectively by compressed air pipe network (4) with the cylinder on blanking device (2), the percussion device (1) controlling to be attached thereto by magnetic valve (3) realizes two or two staggered blankings, namely crust-breaking & baiting point 1 and 4 is controlled respectively, crust-breaking & baiting point 2 and 5, crust-breaking & baiting point 3 and 6, or control crust-breaking & baiting point 1 and 6 respectively, crust-breaking & baiting point 2 and 5, crust-breaking & baiting point 3 and 4, or control crust-breaking & baiting point 1 and 3 respectively, crust-breaking & baiting point 2 and 4, crust-breaking & baiting point 5 and 6.
CN201410014685.5A 2014-01-14 2014-01-14 Electrolysis bath alumina discharge control method Pending CN104775135A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410014685.5A CN104775135A (en) 2014-01-14 2014-01-14 Electrolysis bath alumina discharge control method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410014685.5A CN104775135A (en) 2014-01-14 2014-01-14 Electrolysis bath alumina discharge control method

Publications (1)

Publication Number Publication Date
CN104775135A true CN104775135A (en) 2015-07-15

Family

ID=53616892

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410014685.5A Pending CN104775135A (en) 2014-01-14 2014-01-14 Electrolysis bath alumina discharge control method

Country Status (1)

Country Link
CN (1) CN104775135A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106149006A (en) * 2016-08-28 2016-11-23 包头铝业有限公司 A kind of aluminum cell crust breaking, the control method of blanking system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001006039A1 (en) * 1999-07-19 2001-01-25 Ab Rexroth Mecman Method and device for controlling the movement of a supply and breaking chisel in an aluminium production cell
CN1661136A (en) * 2004-12-22 2005-08-31 沈阳铝镁设计研究院 Crust breaking and loading control system for aluminum cell and control method
CN200964441Y (en) * 2006-05-24 2007-10-24 中国铝业股份有限公司 Prebaked aluminum cell cross crust breaking baiting device
CN201137605Y (en) * 2007-12-03 2008-10-22 西部矿业股份有限公司 Air cylinder

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2001006039A1 (en) * 1999-07-19 2001-01-25 Ab Rexroth Mecman Method and device for controlling the movement of a supply and breaking chisel in an aluminium production cell
CN1661136A (en) * 2004-12-22 2005-08-31 沈阳铝镁设计研究院 Crust breaking and loading control system for aluminum cell and control method
CN200964441Y (en) * 2006-05-24 2007-10-24 中国铝业股份有限公司 Prebaked aluminum cell cross crust breaking baiting device
CN201137605Y (en) * 2007-12-03 2008-10-22 西部矿业股份有限公司 Air cylinder

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106149006A (en) * 2016-08-28 2016-11-23 包头铝业有限公司 A kind of aluminum cell crust breaking, the control method of blanking system

Similar Documents

Publication Publication Date Title
CN101580949B (en) Method for improving stability of aluminum electrolytic bath
CN202705512U (en) Fixing device of positive electrode frame and negative electrode plate in electrolytic cell
CN201473603U (en) Cathode carbon block provided with groove on the surface
CN104775135A (en) Electrolysis bath alumina discharge control method
CN2931501Y (en) Aluminum electrolysis bath cathode heterotype electric steel rod
CN204702818U (en) A kind of energy-saving high-performance rare earth metal and alloy liquid catholyte stove thereof
CN204690126U (en) A kind of device of copper anode rotary electrolysis acceptable cathodic copper
CN205152349U (en) Energy -conserving water electrolysis hydrogen device
CN101256212A (en) Comprehensive analysis testing method for extra-high voltage electric power gold tool
CN102943463B (en) A kind of for soft soil electrochemistry reinforced drum type brake combination electrode and bracing means
CN207554280U (en) A kind of ocean energy comprehensive electric generating and the fertile device of hydrogen
CN102534688A (en) High-current baffleless magnesium electrolytic tank
CN101949035B (en) Novel composite graphitized deformed cathode for aluminium electrolysis
CN201834990U (en) Novel titanium anode plate
CN201354386Y (en) Aluminum electrolysis bath energy-saving cathode block structure
CN203440479U (en) Floating conduction device for continuous electroplating production
CN202730253U (en) Electrolysis bath for preparing rare earth ore extraction acidification water
CN205188454U (en) Electrolysis cell
CN202519344U (en) Aluminum electrolytic cell with cross-configuration irregular cathode structure
CN103603017A (en) Environmental-friendly energy-saving nano electro nickel-plating technology
CN201793763U (en) Novel assembled graphitized special cathode for aluminium electrolysis
CN201501930U (en) Cathode of aluminum cell
MY160577A (en) Method of configuring cathodes of an aluminum reduction cell
CN203256353U (en) Insulated crust breaking hammer mechanism for aluminium-electrolytic cell
CN202808974U (en) Device for preparing hydroxyapatite contained coating on alloy surface by micro-arc oxidation

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
EXSB Decision made by sipo to initiate substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20150715

WD01 Invention patent application deemed withdrawn after publication