GB771144A - Improvements in or relating to the purification of zirconium tetrachloride - Google Patents
Improvements in or relating to the purification of zirconium tetrachlorideInfo
- Publication number
- GB771144A GB771144A GB10953/55A GB1095355A GB771144A GB 771144 A GB771144 A GB 771144A GB 10953/55 A GB10953/55 A GB 10953/55A GB 1095355 A GB1095355 A GB 1095355A GB 771144 A GB771144 A GB 771144A
- Authority
- GB
- United Kingdom
- Prior art keywords
- zirconium tetrachloride
- zirconium
- tetrachloride
- crude
- fused
- 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
- C01—INORGANIC CHEMISTRY
- C01G—COMPOUNDS CONTAINING METALS NOT COVERED BY SUBCLASSES C01D OR C01F
- C01G25/00—Compounds of zirconium
- C01G25/04—Halides
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Inorganic Chemistry (AREA)
- Inorganic Compounds Of Heavy Metals (AREA)
Abstract
Zirconium and hafnium tetrachlorides are purified by heating a fused mixture containing the impure tetrachlorides and a minor amount of at least one alkali metal chloride above the temperature at which the tetrachlorides vaporize and thereafter condensing the evolved purified tetrachlorides. Zirconium tetrachloride and attendant hafnium tetrachloride can thus be freed from metal and metalloid impurities and the content of zirconium oxy chloride decreased. The preferred fused starting mixture contains 88 per cent crude zirconium tetrachloride and 12 per cent potassium chloride which mixture melts at about 215 DEG C. Zirconium tetrachloride sublimes at about 331 DEG C. at atmospheric pressure. According to examples (1) a fused mixture of the zirconium tetrachloride and potassium chloride was heated to 500 DEG C. and the zirconium tetrachloride collected as a crystalline solid. The impurities in the zirconium tetrachloride were reduced from 3000 parts of metallic impurities per million to 193 parts per million. Further examples relate to distillation at 600 and 450 DEG C., and to the use of different alkali metal chlorides and proportions thereof and to the use of mixtures of alkali metal and alkaline earth metal chlorides. A further example (9) describes the re-employment of the fused salt residue after carrying out the zirconium tetrachloride distillation, which residue contains 27.5 parts of zirconium tetrachloride and 12 parts of potassium chloride. To such a residue further crude zirconium chloride is added and the mixture melted and purified zirconium tetrachloride recovered. The crude zirconium tetrachloride can be added to the fused salt residue after the latter has been cooled and pulverized, or while it is in liquid state. Alternatively the fused salt composition may be employed to scrub impurities from the crude tetrachloride. Thus a mixture containing 88 per cent zirconium tetrachloride and 12 per cent potassium chloride may be melted and crude zirconium tetrachloride introduced at about the same rate as purified zirconium tetrachloride is vaporized from the molten salt bath.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US771144XA | 1954-04-16 | 1954-04-16 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB771144A true GB771144A (en) | 1957-03-27 |
Family
ID=22136135
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB10953/55A Expired GB771144A (en) | 1954-04-16 | 1955-04-15 | Improvements in or relating to the purification of zirconium tetrachloride |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB771144A (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2962352A (en) * | 1957-07-26 | 1960-11-29 | Nat Distillers Chem Corp | Purification of zirconium halides |
US5188810A (en) * | 1991-06-27 | 1993-02-23 | Teledyne Industries, Inc. | Process for making niobium oxide |
US5211921A (en) * | 1991-06-27 | 1993-05-18 | Teledyne Industries, Inc. | Process of making niobium oxide |
US5234674A (en) * | 1991-06-27 | 1993-08-10 | Teledyne Industries, Inc. | Process for the preparation of metal carbides |
US5284639A (en) * | 1991-06-27 | 1994-02-08 | Teledyne Industries, Inc. | Method for the preparation of niobium nitride |
US5322548A (en) * | 1991-06-27 | 1994-06-21 | Teledyne Industries, Inc. | Recovery of niobium metal |
US5468464A (en) * | 1991-06-27 | 1995-11-21 | Teledyne Industries, Inc. | Process for the preparation of metal hydrides |
EP1930451A1 (en) * | 2005-07-07 | 2008-06-11 | Nippon Mining & Metals Co., Ltd. | High-purity hafnium, target and thin film comprising high-purity hafnium, and process for producing high-purity hafnium |
CN112357885A (en) * | 2020-12-02 | 2021-02-12 | 中国科学院上海应用物理研究所 | Purification method of single component in chloride molten salt |
CN114835160A (en) * | 2022-05-18 | 2022-08-02 | 江苏南大光电材料股份有限公司 | Preparation method of semiconductor grade hafnium tetrachloride |
-
1955
- 1955-04-15 GB GB10953/55A patent/GB771144A/en not_active Expired
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2962352A (en) * | 1957-07-26 | 1960-11-29 | Nat Distillers Chem Corp | Purification of zirconium halides |
US5188810A (en) * | 1991-06-27 | 1993-02-23 | Teledyne Industries, Inc. | Process for making niobium oxide |
US5211921A (en) * | 1991-06-27 | 1993-05-18 | Teledyne Industries, Inc. | Process of making niobium oxide |
US5234674A (en) * | 1991-06-27 | 1993-08-10 | Teledyne Industries, Inc. | Process for the preparation of metal carbides |
US5284639A (en) * | 1991-06-27 | 1994-02-08 | Teledyne Industries, Inc. | Method for the preparation of niobium nitride |
US5322548A (en) * | 1991-06-27 | 1994-06-21 | Teledyne Industries, Inc. | Recovery of niobium metal |
US5468464A (en) * | 1991-06-27 | 1995-11-21 | Teledyne Industries, Inc. | Process for the preparation of metal hydrides |
EP1930451A1 (en) * | 2005-07-07 | 2008-06-11 | Nippon Mining & Metals Co., Ltd. | High-purity hafnium, target and thin film comprising high-purity hafnium, and process for producing high-purity hafnium |
EP1930451A4 (en) * | 2005-07-07 | 2009-08-19 | Nippon Mining Co | HIGH-PURITY, TARGET AND THIN-FILM HAFNIUM COMPRISING HIGH-PURITY HAFNIUM AND PROCESS FOR PRODUCING HIGH-PURITY HAFNIUM |
CN112357885A (en) * | 2020-12-02 | 2021-02-12 | 中国科学院上海应用物理研究所 | Purification method of single component in chloride molten salt |
CN114835160A (en) * | 2022-05-18 | 2022-08-02 | 江苏南大光电材料股份有限公司 | Preparation method of semiconductor grade hafnium tetrachloride |
CN114835160B (en) * | 2022-05-18 | 2024-03-12 | 江苏南大光电材料股份有限公司 | Preparation method of semiconductor-grade hafnium tetrachloride |
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