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US4185078A Expired / Lapsed US ⏱️ 0.0 years remaining

Extraction process for recovery of rhenium

Assignee: GTE Sylvania Inc
•
Filing: 1978-07-19
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Granted: 1980-01-22
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Expires: 1998-07-19
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Abstract

Abstract A process is disclosed wherein essentially all of the rhenium can be removed from an aqueous solution of molybdenum without the extraction of molybdenum using a particular solvent extraction solution. The extraction solution consists essentially of quaternary ammonium compound and at least about 50 percent by volume of a highly aromatic solvent which dissolves a quaternary ammonium-rhenium complex to the extent of at least 0.1 percent by volume selected from the group consisting of benzene and an aromatic solvent containing primarily lower alkyl benzenes having molecular weights of either 106, 120, 134 or 148 with minor amounts of relatively long chain aliphatic hydrocarbons containing greater than 8 carbon atoms and minor amounts of napthalene.

Inventors

  • 👤 L. Rita Quatrini
  • 👤 Martin B. MacInnis

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-04 01:26
CPC Classifications
C; C22; C22B; C22B61/00; C01; C01G; C01G47/00; C22B3/00; C22B3/20; C22B3/26; C22B3/28; C22B3/288; C22B34/00; C22B34/30; C22B34/34; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 3
Claim 1
Independent Claim 267 words
In a process wherein an aqueous solution containing a relatively high concentration of molybdenum and a relatively low concentration of rhenium is contacted by selective organic extractant solution to preferentially extract the rhenium therefrom without an appreciable extraction of molybdenum into the organic solution and thereafter the organic and aqueous soltuions are separated and the rhenium values are separated from the organic phase, the improvement comprising: (a) providing an organic extractant solution consisting essentially of from at least 0.05 percent to about 0.1 percent by volume of a quaternary ammonium compound of the formula [R 3 (CH 3 )N] + A - , wherein R is an alkyl group having from about 8 to 10 carbon atoms and A is an anion derived from a mineral acid as the active extracting agent and at least 50 percent by volume of an aromatic solvent having as its major constituents, a mixture of alkyl benzenes having molecular weights of either 106, 120, 134 or 148, minor constituents of aliphatic hydrocarbons containing more than 8 carbon atoms and naphthalene, and contacting said organic extractant with an aqueous solution containing molybdenum and rhenium values, wherein the ratio of concentration of rhenium to the concentration of molybdenum is from about 1:2000 to about 1:3000 and the concentration of rhenium is below about 50 mg/liter, (b) stripping essentially all of the rhenium value from said extractant after the aqueous solution has been contacted by said extractant and the organic and aqueous have been separated, and (c) continuously recycling said extractant solution to extract further rhenium values without a substantial loss in extraction capacity.
Claim 2
Dependent Claim 267 words
In a process wherein an aqueous solution containing a relatively high concentration of molybdenum and a relatively low concentration of rhenium is contacted by selective organic extractant solution to preferentially extract the rhenium therefrom without an appreciable extraction of molybdenum into the organic solution and thereafter the organic and aqueous soltuions are separated and the rhenium values are separated from the organic phase, the improvement comprising: (a) providing an organic extractant solution consisting essentially of from at least 0.05 percent to about 0.1 percent by volume of a quaternary ammonium compound of the formula [R 3 (CH 3 )N] + A - , wherein R is an alkyl group having from about 8 to 10 carbon atoms and A is an anion derived from a mineral acid as the active extracting agent and at least 50 percent by volume of an aromatic solvent having as its major constituents, a mixture of alkyl benzenes having molecular weights of either 106, 120, 134 or 148, minor constituents of aliphatic hydrocarbons containing more than 8 carbon atoms and naphthalene, and contacting said organic extractant with an aqueous solution containing molybdenum and rhenium values, wherein the ratio of concentration of rhenium to the concentration of molybdenum is from about 1:2000 to about 1:3000 and the concentration of rhenium is below about 50 mg/liter, (b) stripping essentially all of the rhenium value from said extractant after the aqueous solution has been contacted by said extractant and the organic and aqueous have been separated, and (c) continuously recycling said extractant solution to extract further rhenium values without a substantial loss in extraction capacity.
Claim 3
Dependent Claim 21 words
The process of claim 1 where the ratio of organic extractant to aqueous solution is between about 1:10 to about 10:1.

References Cited (Backward Citations)

US3244475A Cited
US3495934A Cited
US3558268A Cited
US3739057A Cited
US3798305A Cited
US3856915A Cited
US3855385A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-01-21 1983-07-23 1984-01-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-01-21 1987-07-23 1988-01-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-01-21 1991-07-23 1992-01-22 $7700.00 Window Closed / Lapsed

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