RU2002129603A - METHOD FOR RHINIUM EXTRACTION - Google Patents

METHOD FOR RHINIUM EXTRACTION

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Publication number
RU2002129603A
RU2002129603A RU2002129603/15A RU2002129603A RU2002129603A RU 2002129603 A RU2002129603 A RU 2002129603A RU 2002129603/15 A RU2002129603/15 A RU 2002129603/15A RU 2002129603 A RU2002129603 A RU 2002129603A RU 2002129603 A RU2002129603 A RU 2002129603A
Authority
RU
Russia
Prior art keywords
oxidizing agent
solution
hydrochloric acid
exchange resin
hydrogen peroxide
Prior art date
Application number
RU2002129603/15A
Other languages
Russian (ru)
Other versions
RU2323884C2 (en
Inventor
Юлианэ МЕЕЗЕ-МАРКТШЕФФЕЛЬ
Виктор ШТОЛЛЕР
Армин ОЛЬБРИХ
Вольфганг МАТИ
Михаэль ЕРБ
Original Assignee
Х. К. Штарк Гмбх
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
Priority claimed from DE2001155237 external-priority patent/DE10155237A1/en
Application filed by Х. К. Штарк Гмбх filed Critical Х. К. Штарк Гмбх
Publication of RU2002129603A publication Critical patent/RU2002129603A/en
Application granted granted Critical
Publication of RU2323884C2 publication Critical patent/RU2323884C2/en

Links

Claims (10)

1. Способ извлечения рения путем пропускания жидкости, содержащей рений, через сильно основную ионообменную смолу и элюирования адсорбированного рения с помощью высококонцентрированного водного раствора соляной кислоты, отличающийся тем, что ионообменную смолу обрабатывают водным раствором, содержащим окислительное средство.1. A method for extracting rhenium by passing a liquid containing rhenium through a strongly basic ion-exchange resin and eluting adsorbed rhenium with a highly concentrated aqueous hydrochloric acid solution, characterized in that the ion-exchange resin is treated with an aqueous solution containing an oxidizing agent. 2. Способ по п.1, отличающийся тем, что в качестве окислительного средства используют перекись водорода.2. The method according to claim 1, characterized in that hydrogen peroxide is used as the oxidizing agent. 3. Способ по п.2, отличающийся тем, что используют 0,05-4%-ный раствор перекиси водорода.3. The method according to claim 2, characterized in that they use a 0.05-4% solution of hydrogen peroxide. 4. Способ по одному из пп.1-3, отличающийся тем, что элюирование осуществляют 8-12 молярным раствором соляной кислоты.4. The method according to one of claims 1 to 3, characterized in that the elution is carried out with an 8-12 molar solution of hydrochloric acid. 5. Способ по одному из пп.1-4, отличающийся тем, что окислительное средство добавляют к раствору соляной кислоты.5. The method according to one of claims 1 to 4, characterized in that the oxidizing agent is added to the hydrochloric acid solution. 6. Способ по одному из пп.1-5, отличающийся тем, что насыщенную ионообменную смолу перед элюированием обрабатывают водным раствором окислительного средства.6. The method according to one of claims 1 to 5, characterized in that the saturated ion-exchange resin is treated with an aqueous solution of an oxidizing agent before elution. 7. Способ по одному из пп.1-6, отличающийся тем, что элюирование проводят многоступенчато и, по крайней мере, перед последней ступенью проводят промежуточную обработку ионообменной смолы раствором окислительного средства.7. The method according to one of claims 1 to 6, characterized in that the elution is carried out in stages and, at least before the last stage, an intermediate treatment of the ion exchange resin with a solution of an oxidizing agent is carried out. 8. Способ по п.5, отличающийся тем, что раствор соляной кислоты содержит 0,05-0,25 вес.% перекиси водорода в растворенном виде.8. The method according to claim 5, characterized in that the hydrochloric acid solution contains 0.05-0.25 wt.% Hydrogen peroxide in dissolved form. 9. Способ по одному из пп.1-8, отличающийся тем, что раствор окислительного средства для предварительной и/или промежуточной обработки содержит 0,5-3,5 вес.% перекиси водорода.9. The method according to one of claims 1 to 8, characterized in that the solution of the oxidizing agent for preliminary and / or intermediate processing contains 0.5-3.5 wt.% Hydrogen peroxide. 10. Способ по одному из пп.1-9, отличающийся тем, что элюат уменьшают в объеме перегонкой, отогнанный хлористый водород конденсируют для дальнейшего использования в качестве элюирующего средства, рений собирают в кубовой жидкости и затем перерабатывают известными способами.10. The method according to one of claims 1 to 9, characterized in that the eluate is reduced in volume by distillation, the distilled hydrogen chloride is condensed for further use as an eluting agent, rhenium is collected in bottoms and then processed by known methods.
RU2002129603A 2001-11-09 2002-11-06 Method for rhenium isolation RU2323884C2 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE10155237.8 2001-11-09
DE2001155237 DE10155237A1 (en) 2001-11-09 2001-11-09 Process for the production of rhenium

Publications (2)

Publication Number Publication Date
RU2002129603A true RU2002129603A (en) 2004-05-10
RU2323884C2 RU2323884C2 (en) 2008-05-10

Family

ID=7705295

Family Applications (1)

Application Number Title Priority Date Filing Date
RU2002129603A RU2323884C2 (en) 2001-11-09 2002-11-06 Method for rhenium isolation

Country Status (12)

Country Link
US (1) US6936090B2 (en)
EP (1) EP1310459B1 (en)
JP (1) JP2003201527A (en)
KR (1) KR20030038510A (en)
CN (1) CN1232444C (en)
AT (1) ATE305438T1 (en)
CA (1) CA2411345A1 (en)
DE (2) DE10155237A1 (en)
MX (1) MXPA02011037A (en)
PE (1) PE20030503A1 (en)
RU (1) RU2323884C2 (en)
TW (1) TW200303791A (en)

Families Citing this family (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE102006030731A1 (en) * 2006-06-30 2008-01-03 H.C. Starck Gmbh Recycling of superalloys
US8187561B2 (en) * 2007-12-05 2012-05-29 Ames Goldsmith Corporation Processes and systems for recovering catalyst promoter from catalyst substrates
CN100489131C (en) * 2007-12-12 2009-05-20 安泰科技股份有限公司 Method for manufacturing difficult-to-form pure rhenium sheet
US8057572B2 (en) * 2008-03-07 2011-11-15 Exxonmobil Research And Engineering Company Metal recovery
CA2756337C (en) 2009-03-13 2016-02-23 Neo Performance Materials Limited Rhenium recovery
US20100263490A1 (en) 2009-04-16 2010-10-21 Freeport-Mcmoran Copper & Gold Inc. Methods and systems for recovering rhenium from a copper leach
US8383070B2 (en) * 2010-03-16 2013-02-26 World Resources Company Method for recovering rhenium and other metals from rhenium-bearing materials
AU2014201865B2 (en) * 2011-06-30 2016-04-28 Kabushiki Kaisha Toshiba Process for producing rare metal
CN102251107B (en) * 2011-07-06 2013-04-17 湖南稀土金属材料研究院 Method for treating rhenium-containing raw material
CN102703699B (en) * 2012-06-26 2013-12-04 西部鑫兴金属材料有限公司 Recycling method of acid waste liquid after treatment of high-lead rhenium-containing molybdenum concentrate
CN102703737B (en) * 2012-06-28 2013-08-07 青岛阿库卡稀有金属有限公司 Method for extracting and separating rhenium from rhenium-containing slag
RU2637452C1 (en) * 2016-10-31 2017-12-04 Федеральное государственное бюджетное учреждение науки Институт металлургии Уральского отделения Российской академии наук (ИМЕТ УрО РАН) Method for extracting rhenium from water solutions
KR101896799B1 (en) * 2016-11-30 2018-09-07 현대자동차주식회사 Method of recovering and converting rhenium oxide in dibutyl muconate manufacturing process
CN110846510B (en) * 2019-12-19 2021-08-10 安徽工业大学 Method for efficiently and selectively adsorbing and recovering rhenium and mercury from copper smelting multi-element mixed waste acid

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE260227C (en)
DE155825C (en)
US2876065A (en) 1955-04-11 1959-03-03 Kennecott Copper Corp Process for producing pure ammonium perrhenate and other rhenium compounds
US2945743A (en) 1958-02-27 1960-07-19 Kennecott Copper Corp Process for purifying impure rhenium-bearing solutions by ion exchange
US3244475A (en) * 1962-10-31 1966-04-05 Philip E Churchward Solvent extraction process for separating rhenium from molybdenum
US3458277A (en) * 1966-07-21 1969-07-29 Kennecott Copper Corp Process for the recovery of molybdenum values as high purity ammonium paramolybdate from impure molybdenum-bearing solution,with optional recovery of rhenium values if present
US3558268A (en) 1967-11-13 1971-01-26 Kennecott Copper Corp Process for recovering rhenium values from ion exchange materials
DE2021631B2 (en) 1970-05-02 1971-11-18 Heraeus Gmbh W C CLEANING PROCEDURES FOR RHENIUM SOLUTIONS
US3672874A (en) 1970-11-12 1972-06-27 Universal Oil Prod Co Recovery of rhenium values from a spent catalyst
US3984478A (en) * 1975-05-27 1976-10-05 Universal Oil Products Company Hydroformylation process
DE2836641A1 (en) 1977-09-27 1979-04-05 Leuna Werke Veb METHOD FOR OBTAINING RHENIUM COMPOUNDS FROM RHENIUM-CONTAINING SOLUTIONS
DE2836632A1 (en) 1977-09-27 1979-04-05 Leuna Werke Veb METHOD FOR RECOVERY OF RHENIUM
DD155825A1 (en) 1979-04-12 1982-07-07 Karl Becker METHOD FOR THE ELUTION OF RHENIUM-PAINTED SORBED RESINS ON ION EXCHANGER RESINS
US4557906A (en) * 1984-11-07 1985-12-10 Gte Products Corporation Recovery of rhenium
DD260227A1 (en) 1987-05-04 1988-09-21 Akad Wissenschaften Ddr METHOD FOR THE ELUTION OF RHENIUM FROM ANION EXCHANGERS
US5116415A (en) * 1989-09-25 1992-05-26 Aqs, Inc. Metal value recovery or removal from aqueous media

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