GB744396A - Process for the preparation of substantially pure titanium metal - Google Patents

Process for the preparation of substantially pure titanium metal

Info

Publication number
GB744396A
GB744396A GB27224/53A GB2722453A GB744396A GB 744396 A GB744396 A GB 744396A GB 27224/53 A GB27224/53 A GB 27224/53A GB 2722453 A GB2722453 A GB 2722453A GB 744396 A GB744396 A GB 744396A
Authority
GB
United Kingdom
Prior art keywords
titanium
anode
cell
halides
cap
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
GB27224/53A
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.)
Norton Grinding Wheel Co Ltd
Original Assignee
Norton Grinding Wheel 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 Norton Grinding Wheel Co Ltd filed Critical Norton Grinding Wheel Co Ltd
Publication of GB744396A publication Critical patent/GB744396A/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
    • C25C3/26Electrolytic production, recovery or refining of metals by electrolysis of melts of titanium, zirconium, hafnium, tantalum or vanadium
    • C25C3/28Electrolytic production, recovery or refining of metals by electrolysis of melts of titanium, zirconium, hafnium, tantalum or vanadium of titanium

Landscapes

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

Abstract

744,396. Electrolytic production of titanium. NORTON GRINDING WHEEL CO., Ltd. Oct. 5, 1953 [Oct. 4, 1952], No. 27224/53. Class 41. Pure titanium is produced as a powder by electrolytic deposition in a cell containing one or more fused halides, preferably chlorides, of lithium, sodium, potassium, magnesium, calcium, and aluminium, and titanium carbide isolated from the cathode, e.g. as the anode. preferably the titanium carbide is in powder form in a cup surrounding the anode but it may be a sintered rod forming the anode. The cell is run at 500-600‹ C. and argon is passed continuously through the cell while chlorine may also be passed continuously to prevent deposition of the metals of the halides, especially magnesium, calcium, and aluminium which are difficult to remove from titanium. If desired powdered titanium carbide may be converted to titanium tetrachloride by passing chlorine into the heated cell before electrolysis. As shown, the cell housed in a container 22 packed with heat insulating material 31 and surrounded by an electric heater 28 comprises a tubular cathode 1 of titanium, nickel, or stainless steel closed at the lower end and screwed at the upper end into a steel coverplate 14 resting on an asbestos board 21 forming the lid of the container. The plate 14 carries a threaded steel plug 13 in which rests a ceramic cap 10 supporting a porous ceramic tubular partition 3 which is gripped by an asbestos washer for the plug 13 and from which depends a porous cup 4 containing powdered titanium carbide. A hollow carbon anode 7 surrounded for most of its length by a non-porous ceramic tube 8 passes through the cap 10, anode and tube being supported by releasable collars resting on the cap. Argon is passed into the cell through the tube 50 and chlorine is supplied through the hollow anode, a slow leak occurring around the cap 10. If chlorine is supplied continuously the top of the cell may be modified to collect and re-cycle the gas. A tube 57 is provided in the casing for a thermoelectric thermometer. The ceramics used may be different forms of alumina. If a sintered titanium rod is used as the anode, the sleeve 8 and the cup 4 may be omitted. When deposition of titanium is complete and before the melt has set the plug 13 and its associated assembly is replaced by a similar plug carrying an airtight cap through which a siphon tube passes so that by increasing the argon pressure the bulk of the liquid salt may be drawn off. When the mixture of halides and titanium in powder form has set it is scraped out and the titanium is freed from the halides either by vacuum distillation in the case of lithium, sodium, and potassium halides or by organic solvents in the case of magnesium, calcium, aluminium, and lithium halides. The resulting titanium sponge metal is consolidated into ingots by heating in an argon atmosphere and casting into graphite moulds or pressing into blocks.
GB27224/53A 1952-10-04 1953-10-05 Process for the preparation of substantially pure titanium metal Expired GB744396A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US744396XA 1952-10-04 1952-10-04

Publications (1)

Publication Number Publication Date
GB744396A true GB744396A (en) 1956-02-08

Family

ID=22119558

Family Applications (1)

Application Number Title Priority Date Filing Date
GB27224/53A Expired GB744396A (en) 1952-10-04 1953-10-05 Process for the preparation of substantially pure titanium metal

Country Status (1)

Country Link
GB (1) GB744396A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2817631A (en) * 1956-03-23 1957-12-24 Chicago Dev Corp Refining titanium alloys
US2904491A (en) * 1956-05-02 1959-09-15 Nat Lead Co Apparatus for producing refractory metal
US2970092A (en) * 1956-04-24 1961-01-31 Minnesota Mining & Mfg Process for the production of fluorinecontaining compounds
US2970093A (en) * 1956-04-24 1961-01-31 Minnesota Mining & Mfg Process for the production of fluorinecontaining compounds
US3002846A (en) * 1956-07-02 1961-10-03 Bayer Ag Process for the manufacture of inorganic pigments
DE1147761B (en) * 1956-06-29 1963-04-25 Dr Ichiro Egami Method and device for the production of titanium by reducing titanium tetrachloride with liquid magnesium produced by means of fused-salt electrolysis
US3203881A (en) * 1952-07-16 1965-08-31 British Titan Products Production of metallic halides
CN103484898A (en) * 2013-10-10 2014-01-01 宝纳资源控股(集团)有限公司 Vacuum high-temperature continuous electrolytic furnace system and electrolytic method
CN104928720A (en) * 2015-07-13 2015-09-23 攀钢集团攀枝花钢铁研究院有限公司 Electrolyzing method for titanium soluble anode
CN106835203A (en) * 2016-12-26 2017-06-13 宝纳资源控股(集团)有限公司 The purifier and method of a kind of fused salt

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3203880A (en) * 1952-07-16 1965-08-31 British Titan Products Electrolytic production of titanium tetrahalides
US3203881A (en) * 1952-07-16 1965-08-31 British Titan Products Production of metallic halides
US2817631A (en) * 1956-03-23 1957-12-24 Chicago Dev Corp Refining titanium alloys
US2970092A (en) * 1956-04-24 1961-01-31 Minnesota Mining & Mfg Process for the production of fluorinecontaining compounds
US2970093A (en) * 1956-04-24 1961-01-31 Minnesota Mining & Mfg Process for the production of fluorinecontaining compounds
US2904491A (en) * 1956-05-02 1959-09-15 Nat Lead Co Apparatus for producing refractory metal
DE1147761C2 (en) * 1956-06-29 1963-11-07 Dr Ichiro Egami Process and device for the production of titanium by reducing titanium tetrachloride with liquid magnesium produced by means of fused salt electrolysis
DE1147761B (en) * 1956-06-29 1963-04-25 Dr Ichiro Egami Method and device for the production of titanium by reducing titanium tetrachloride with liquid magnesium produced by means of fused-salt electrolysis
US3002846A (en) * 1956-07-02 1961-10-03 Bayer Ag Process for the manufacture of inorganic pigments
CN103484898A (en) * 2013-10-10 2014-01-01 宝纳资源控股(集团)有限公司 Vacuum high-temperature continuous electrolytic furnace system and electrolytic method
CN103484898B (en) * 2013-10-10 2016-04-27 宝纳资源控股(集团)有限公司 A kind of vacuum high-temperature continuous electrolysis furnace system and electrolysis process
CN104928720A (en) * 2015-07-13 2015-09-23 攀钢集团攀枝花钢铁研究院有限公司 Electrolyzing method for titanium soluble anode
CN104928720B (en) * 2015-07-13 2018-08-14 成都先进金属材料产业技术研究院有限公司 A kind of electrolytic method of titanium soluble anode
CN106835203A (en) * 2016-12-26 2017-06-13 宝纳资源控股(集团)有限公司 The purifier and method of a kind of fused salt
CN106835203B (en) * 2016-12-26 2019-05-31 宝纳资源控股(集团)有限公司 A kind of purification device and method of fused salt

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