GB784695A - Improvements in or relating to electrolytic cells for the production of aluminium - Google Patents

Improvements in or relating to electrolytic cells for the production of aluminium

Info

Publication number
GB784695A
GB784695A GB1054851A GB1054851A GB784695A GB 784695 A GB784695 A GB 784695A GB 1054851 A GB1054851 A GB 1054851A GB 1054851 A GB1054851 A GB 1054851A GB 784695 A GB784695 A GB 784695A
Authority
GB
United Kingdom
Prior art keywords
per cent
temperature
carbon content
free carbon
benzene
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
GB1054851A
Inventor
Charles Eric Ransley
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.)
British Aluminum Co Ltd
Original Assignee
British Aluminum 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 British Aluminum Co Ltd filed Critical British Aluminum Co Ltd
Publication of GB784695A publication Critical patent/GB784695A/en
Priority to US125318A priority Critical patent/US3202600A/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
    • C25C3/16Electric current supply devices, e.g. bus bars
    • 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)
  • Carbon And Carbon Compounds (AREA)

Abstract

The free carbon content in zirconium carbide is reduced by a process similar to that described in Specification 784,697 with respect to titanium carbide, but the final firing temperature is 2700 DEG C. Specification 784,696 also is referred to.ALSO:A compact mass of titanium carbide for use as a cathode in a fused-electrolytic cell for obtaining aluminium is made by first mixing the powdered material having a mean particle diameter of 1-2 microns with a binder such as 1 per cent of paraffin wax dissolved in benzene. This is heated to evaporate the benzene and melt the wax and compacted with a pressure 0.5-5 tons per sq. inch. Compacting may be effected between male and female dies at an ordinary or an elevated temperature, or the material may be p extruded into the desired shape. The mass is then prefired in vacuum to a temperature of 1100 DEG C. If not already formed to the desired shape it may be worked by sawing, filing or like operation. It is then fired in vacuum at 1600 DEG C., or in a neutral gas, e.g. hydrogen. A compact mass of zirconium carbide may be similarly made, the prefiring temperature being in this case 1600 DEG C. and the subsequent firing temperature 2200 DEG C. The free carbon content of the product must be below 0.5 per cent, preferably below 0.1 per cent. If commercial titanium carbide powder containing 1-2 per cent of carbon with some titanium oxide is employed the free carbon content is reduced by mixing with the powder about 2-3 per cent of alumina before the operation above described, and employing higher sintering temperatures. Specifications 784,696 and 784,697 are referred to.ALSO:A compact mass of titanium carbide for use as a cathode in a fused-electrolytic cell for obtaining aluminium is made by first mixing the powdered material having a mean particle diameter of 1-2 microns with a binder such as 1 per cent of paraffin wax dissolved in benzene. This is heated to evaporate the benzene and melt the wax and compacted with a pressure 0,5-5 tons per sq. inch. Compacting may be effected between male and female dies at an ordinary or an elevated temperature, or the material may be extruded into the desired shape. The mass is then pre-fired in vacuum to a temperature of 1100 DEG C. If not already formed to the desired shape it may be worked by sawing, filing or like operation. It is then fired in vacuum at 1600 DEG C., or in a neutral gas, e.g., hydrogen. A compact mass of zirconium carbide may be similarly made, the pre-firing temperature being in this case 1600 DEG C. and the subsequent firing temperature 2200 DEG C. The free carbon content of the product must be below 0,5 per cent, preferably below 0,1 per cent. If commercial titanium carbide powder containing 1-2 per cent of carbon with some titanium oxide is employed the free carbon content is reduced by mixing with the powder about 2-3 per cent of alumina before the operations above described, and employing higher sintering temperatures. Specifications 784,696 and 784,697 are referred to.
GB1054851A 1951-05-04 1951-05-04 Improvements in or relating to electrolytic cells for the production of aluminium Expired GB784695A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US125318A US3202600A (en) 1951-05-04 1961-06-12 Current conducting element for aluminum reduction cells

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
GB1849051A GB784696A (en) 1951-08-03 1951-08-03 Improvements in or relating to electrolytic cells for the production of aluminium

Publications (1)

Publication Number Publication Date
GB784695A true GB784695A (en) 1957-10-16

Family

ID=10302310

Family Applications (2)

Application Number Title Priority Date Filing Date
GB1054851A Expired GB784695A (en) 1951-05-04 1951-05-04 Improvements in or relating to electrolytic cells for the production of aluminium
GB1849051A Expired GB784696A (en) 1951-08-03 1951-08-03 Improvements in or relating to electrolytic cells for the production of aluminium

Family Applications After (1)

Application Number Title Priority Date Filing Date
GB1849051A Expired GB784696A (en) 1951-08-03 1951-08-03 Improvements in or relating to electrolytic cells for the production of aluminium

Country Status (4)

Country Link
CH (2) CH299434A (en)
DE (1) DE1092215B (en)
FR (2) FR1061906A (en)
GB (2) GB784695A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2959527A (en) * 1957-01-05 1960-11-08 Montedison Spa Self-restoring anode in multi-cell furnaces particularly for the electrolytic production of aluminum
DE1115467B (en) * 1958-07-24 1961-10-19 Montecatini Sozieta Generale P Furnace for the production of aluminum by fusible electrolysis
EP0042658A2 (en) * 1980-06-23 1981-12-30 KAISER ALUMINUM & CHEMICAL CORPORATION Aluminum reduction cell electrode
US4333813A (en) 1980-03-03 1982-06-08 Reynolds Metals Company Cathodes for alumina reduction cells

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES203316A1 (en) * 1951-05-04 1952-07-01 British Aluminium Co Ltd Current conducting element for aluminum production cells
NL109009C (en) * 1954-01-19
BE548465A (en) * 1955-06-08
BE549859A (en) * 1955-07-28
US2915442A (en) * 1955-11-28 1959-12-01 Kaiser Aluminium Chem Corp Production of aluminum
GB898602A (en) * 1957-05-01 1962-06-14 British Aluminium Co Ltd Improvements in or relating to electrolytic cells for the production of metals
US3151053A (en) * 1958-06-12 1964-09-29 Kaiser Aluminium Chem Corp Metallurgy
US3081254A (en) * 1958-06-24 1963-03-12 Kaiser Aluminium Chem Corp Electrolytic cell structure
US3156639A (en) * 1961-08-17 1964-11-10 Reynolds Metals Co Electrode

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE622522C (en) * 1932-08-06 1935-11-29 Metallwerk Plansee G M B H Electrical contact material that contains one or more carbides in addition to one or more lower melting and softer metals

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2959527A (en) * 1957-01-05 1960-11-08 Montedison Spa Self-restoring anode in multi-cell furnaces particularly for the electrolytic production of aluminum
DE1115467B (en) * 1958-07-24 1961-10-19 Montecatini Sozieta Generale P Furnace for the production of aluminum by fusible electrolysis
US3067124A (en) * 1958-07-24 1962-12-04 Montedison Spa Furnace for fused-bath electrolysis, particularly for aluminum production from alo
US4333813A (en) 1980-03-03 1982-06-08 Reynolds Metals Company Cathodes for alumina reduction cells
EP0042658A2 (en) * 1980-06-23 1981-12-30 KAISER ALUMINUM & CHEMICAL CORPORATION Aluminum reduction cell electrode
EP0042658A3 (en) * 1980-06-23 1982-03-10 KAISER ALUMINUM & CHEMICAL CORPORATION Aluminum reduction cell electrode

Also Published As

Publication number Publication date
FR1061906A (en) 1954-04-16
CH299434A (en) 1954-06-15
DE1092215B (en) 1960-11-03
GB784696A (en) 1957-10-16
FR1064743A (en) 1954-05-17
CH301030A (en) 1954-08-31

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