GB744396A - Process for the preparation of substantially pure titanium metal - Google Patents
Process for the preparation of substantially pure titanium metalInfo
- 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
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25C—PROCESSES FOR THE ELECTROLYTIC PRODUCTION, RECOVERY OR REFINING OF METALS; APPARATUS THEREFOR
- C25C3/00—Electrolytic production, recovery or refining of metals by electrolysis of melts
- C25C3/26—Electrolytic production, recovery or refining of metals by electrolysis of melts of titanium, zirconium, hafnium, tantalum or vanadium
- C25C3/28—Electrolytic 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.
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)
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 |
-
1953
- 1953-10-05 GB GB27224/53A patent/GB744396A/en not_active Expired
Cited By (15)
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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