GB919528A - Process for producing high purity rhenium and its compounds - Google Patents
Process for producing high purity rhenium and its compoundsInfo
- Publication number
- GB919528A GB919528A GB674361A GB674361A GB919528A GB 919528 A GB919528 A GB 919528A GB 674361 A GB674361 A GB 674361A GB 674361 A GB674361 A GB 674361A GB 919528 A GB919528 A GB 919528A
- Authority
- GB
- United Kingdom
- Prior art keywords
- per
- acid
- cation exchanger
- rhenic
- rhenium
- 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
- C22—METALLURGY; FERROUS OR NON-FERROUS ALLOYS; TREATMENT OF ALLOYS OR NON-FERROUS METALS
- C22B—PRODUCTION AND REFINING OF METALS; PRETREATMENT OF RAW MATERIALS
- C22B61/00—Obtaining metals not elsewhere provided for in this subclass
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Manufacturing & Machinery (AREA)
- Materials Engineering (AREA)
- Mechanical Engineering (AREA)
- Metallurgy (AREA)
- Organic Chemistry (AREA)
- Manufacture And Refinement Of Metals (AREA)
Abstract
Per-rhenic acid, containing cationic metal contaminants is purified by contacting an aqueous solution thereof with a cation exchanger in the hydrogen form and recovering per-rhenic acid pure from the effluent, the cations being retained by the cation exchanger. Rhenium values are converted to per-rhenic acid by combustion in oxygen, condensing the oxides, mainly rhenium heptoxide, lixiviating said sublimate with distilled water, filtering and subjecting the filtrate to contact with a bed of cation exchanger. The effluent of purified per-rhenic acid may be neutralized with ammonia; ammonium per-rhenate may be crystallized and may be reduced by heating with hydrogen. The metal may be used for manufacturing electronic components by powder metallurgy. The mother liquor from which ammonium per-rhenate has been recovered may be recirculated in the process by adding it to a further batch of rhenium values. The cation exchanger may be regenerated by contact with a non-oxidizing mineral acid, e.g. 12% hydrochloric acid. The examples relate to the removal of impurities which include potassium, iron, copper, magnesium and aluminium ions; alkali and alkaline earth metal ions may also be removed by the process.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US2604360A | 1960-05-02 | 1960-05-02 |
Publications (1)
Publication Number | Publication Date |
---|---|
GB919528A true GB919528A (en) | 1963-02-27 |
Family
ID=21829557
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
GB674361A Expired GB919528A (en) | 1960-05-02 | 1961-02-23 | Process for producing high purity rhenium and its compounds |
Country Status (1)
Country | Link |
---|---|
GB (1) | GB919528A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114214528A (en) * | 2021-12-06 | 2022-03-22 | 洛阳双罗铼材料科技有限公司 | Preparation method of high-purity ammonium rhenate |
CN115072789A (en) * | 2022-08-08 | 2022-09-20 | 中国地质科学院郑州矿产综合利用研究所 | Preparation method of high-purity ammonium rhenate |
CN115072789B (en) * | 2022-08-08 | 2024-06-07 | 中国地质科学院郑州矿产综合利用研究所 | Preparation method of high-purity ammonium rhenate |
-
1961
- 1961-02-23 GB GB674361A patent/GB919528A/en not_active Expired
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN114214528A (en) * | 2021-12-06 | 2022-03-22 | 洛阳双罗铼材料科技有限公司 | Preparation method of high-purity ammonium rhenate |
CN115072789A (en) * | 2022-08-08 | 2022-09-20 | 中国地质科学院郑州矿产综合利用研究所 | Preparation method of high-purity ammonium rhenate |
CN115072789B (en) * | 2022-08-08 | 2024-06-07 | 中国地质科学院郑州矿产综合利用研究所 | Preparation method of high-purity ammonium rhenate |
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