GB208717A - Improvements in or relating to electrolytic refining of aluminium - Google Patents

Improvements in or relating to electrolytic refining of aluminium

Info

Publication number
GB208717A
GB208717A GB31951/23A GB3195123A GB208717A GB 208717 A GB208717 A GB 208717A GB 31951/23 A GB31951/23 A GB 31951/23A GB 3195123 A GB3195123 A GB 3195123A GB 208717 A GB208717 A GB 208717A
Authority
GB
United Kingdom
Prior art keywords
aluminium
per cent
anode
fluoride
alloy
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
Application number
GB31951/23A
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.)
Howmet Aerospace Inc
Original Assignee
Aluminum Company of America
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 Aluminum Company of America filed Critical Aluminum Company of America
Publication of GB208717A publication Critical patent/GB208717A/en
Expired 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
    • C25C3/24Refining
    • 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
    • C25C3/08Cell construction, e.g. bottoms, walls, cathodes

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

208,717. Aluminum Co. of America, (Assignees of Hoopes, W.). Dec. 21, 1922, [Convention date]. Void [Published under Sect. 91 of the Act]. Aluminium, obtaining. - The charge of an electric furnace for obtaining pure aluminium comprises a layer 14 of a relatively dense aluminium alloy constituting the anode, an intermediate layer 20 of fused fluorides, and an upper layer 21 of aluminium constituting the cathode. Refined aluminium is withdraw from time to time by a notch 26, provided with a refractory plug 26 and impoverished anode alloy is withdrawn by a tapping plug 29. Fresh alloy may be supplied through a carbon funnel let down into the anode layer. The furnace comprises a carbon base 13 having a bowllike cavity and enclosed together with a bottom heat-insulating layer 12 of bauxite in a steel shell 11. The shell 11 is provided with a water-cooled ring 19 surmounted by and insulated from a water cooled ring 18. An insulating refractory lining 17 is frozen on the shell walls by the cooled rings and an insulating refractory top, crust 22 which may be of both ingredients is formed above the cathode. The anode is connected to the positive supply conductor by a bus-bar 15 and distributor plates 16 and the cathode is connected to the negative supply conductor by graphite plates 23 and rods 24. The anode alloy may consist of aluminium and copper in the proportion of 60 to 40 and silicon up to 10 per cent. Iron though not advantageous may be present up to 10 per cent. The electrolyte preferably consists of aluminium fluoride 33 per cent, sodium fluoride 30 per cent, barium fluoride 35 per cent and alumina 2 per cent. The barium fluoride may be replaced wholly or in part by strontium fluoride. If alumina accumulates in the bath it may freeze on to the lining so as to choke the cell rendering it necessary to break away a portion of the lining and form a new one. To prevent this, a portion of the bath may be removed from time to time and replaced by material free from alumina. A pressure of 7 volts and current density between 900 and 1400, preferably 1200, amps per sq. foot of anode are employed, the working temperature being about 950‹ C. Aluminium containing not more than 0.15 per cent or even 0.1 per cent of impurities may be obtained, the impurities being iron silicon and copper. Such aluminium is said to be characterised by a high degree of softness, ductibilty, malleability and strength and by high resistance to attack by dilute hydrochloric and other acids. Its melting point is 659‹.5 + 0.3 C. Its specific resistance at 20‹ C. is 2.7 michroms per cur. cube. Its appearance is silvery and it retains its lustre for a long period. It is specially suitable for making collapsable tubes.
GB31951/23A 1922-12-21 1923-12-20 Improvements in or relating to electrolytic refining of aluminium Expired GB208717A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US608282A US1534315A (en) 1922-12-21 1922-12-21 Electrolytically-refined aluminum and articles made therefrom

Publications (1)

Publication Number Publication Date
GB208717A true GB208717A (en) 1925-04-20

Family

ID=24435790

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31951/23A Expired GB208717A (en) 1922-12-21 1923-12-20 Improvements in or relating to electrolytic refining of aluminium

Country Status (3)

Country Link
US (1) US1534315A (en)
FR (1) FR575467A (en)
GB (1) GB208717A (en)

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2659046A (en) * 1948-10-19 1953-11-10 Arps Jan Jacob Geophysical exploration using radioactive material
US3018233A (en) * 1960-02-09 1962-01-23 Manganese Chemicals Corp Producing manganese by fused salt electrolysis, and apparatus therefor
US3432422A (en) * 1961-11-24 1969-03-11 Hooker Chemical Corp Current conducting members for electrolytic cell
US4780186A (en) * 1987-06-22 1988-10-25 Aluminum Company Of America Lithium transport cell process
US4849072A (en) * 1987-09-21 1989-07-18 Aluminum Company Of America Electrolytic process for recovering lithium from aluminum-lithium alloy scrap
US4973390A (en) * 1988-07-11 1990-11-27 Aluminum Company Of America Process and apparatus for producing lithium from aluminum-lithium alloy scrap in a three-layered lithium transport cell
US5071523A (en) * 1989-10-13 1991-12-10 Aluminum Company Of America Two stage lithium transport process
US6440294B1 (en) * 1999-09-29 2002-08-27 Alcoa Inc. Crust hole repair for electrolytic cells
US20070034646A1 (en) * 2005-08-12 2007-02-15 Howmedica Osteonics Corp. Foil monomer container and dispenser

Also Published As

Publication number Publication date
FR575467A (en) 1924-07-30
US1534315A (en) 1925-04-21

Similar Documents

Publication Publication Date Title
US5024737A (en) Process for producing a reactive metal-magnesium alloy
US3502553A (en) Process and apparatus for the electrolytic continuous direct production of refined aluminum and of aluminum alloys
GB208717A (en) Improvements in or relating to electrolytic refining of aluminium
US1534316A (en) Production of metallic aluminum from impure materials
US1534322A (en) Electrolytic cell and method of lining the same
US1535458A (en) Method of and apparatus for electrolytic refining
US1534318A (en) Electrolytic refining of aluminum
US3202600A (en) Current conducting element for aluminum reduction cells
GB666281A (en) Improvements relating to the production of magnesium-lithium alloys
US1782616A (en) Electrolytic apparatus for refining aluminum and for like processes
US2451490A (en) Production of aluminum
GB1046705A (en) Improvements in or relating to the operation of electrolytic reduction cells for theproduction of aluminium
US1534319A (en) Refining aluminum electrolytically with fused electrolytes
US1572253A (en) Method of starting electrolytic cells
US3700581A (en) Cryolitic vat for the production of aluminum by electrolysis
US3756929A (en) Method of operating an aluminium oxide reduction cell
CN208362485U (en) A kind of energy-saving Wan An training rare earth molten salt electrolytic system
GB208712A (en) Improvements in or relating to methods of lining electrolytic cells for refining metals
CN105177631B (en) Electrorefining prepares the method and electrolytic cell of rafifinal
US1534321A (en) Method of lining cells for electrolytic refining
US3503857A (en) Method for producing magnesium ferrosilicon
GB812817A (en) Electrolytic production of titanium
GB208715A (en) Improvements in or relating to the production of aluminium
Frary The electrolytic production of aluminum
US3736244A (en) Electrolytic cells for the production of aluminum