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US4287159A Expired / Lapsed US ⏱️ 0.0 years remaining

Extraction process for the recovery of tungsten from low level sources

Assignee: Osram Sylvania Inc
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Filing: 1980-09-15
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Granted: 1981-09-01
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Expires: 2000-09-15
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Abstract

Abstract A process for recovering tungsten from low level sources such as naturally occurring brines in a form substantially free of contaminating boron comprises adjusting the pH of the source solution to a value below about pH 8, contacting the pH-adjusted solution with an ion exchange resin, preferentially eluting the tungsten values in an aqueous eluate, extracting the eluate solution with an organic extractant comprising o-mercaptobenzoic acid, a quaternary alkylammonium salt and an inert organic solvent, and stripping the tungsten-loaded organic extractant solution with an aqueous basic stripping solution.

Inventors

  • 👤 Samuel Natansohn
  • 👤 Sophia R. Su

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-08 12:10
CPC Classifications
C; C22; C22B; C22B3/00; C22B3/20; C22B3/26; C22B3/32; C01; C01G; C01G41/00; C01G41/003; C22B3/262; C22B3/28; C22B3/288; C22B3/34; C22B3/42; Y; Y02; Y02P; Y02P10/00; Y02P10/20; Y10; Y10S; Y10S423/00; Y10S423/09; Y10S423/14

Claims Analysis

Total Claims: 15
Claim 1
Independent Claim 200 words
A process for recovering tungsten substantially free of contaminating boron from aqueous media containing tungsten and boron comprising the steps of: (a) adjusting the pH of said aqueous medium to a value below about pH 8; (b) contacting the pH-adjusted aqueous medium with an ion exchange resin to load the resin with tungsten and boron values from said aqueous medium; (c) eluting the loaded resin with an aqueous eluant solution to selectively recover a portion of the tungsten from said loaded resin; (d) adjusting the pH of the tungsten-containing aqueous eluate solution to a value below about pH 3; (e) contacting the pH-adjusted aqueous eluate solution with an organic extractant solution comprising o-mercaptobenzoic acid, a quaternary alkylammonium salt, and an inert organic solvent to transfer a portion of the tungsten values to the organic extractant solution; (f) contacting the tungsten-containing organic extractant solution with an aqueous stripping solution to transfer a portion of the tungsten values to said aqueous stripping solution and to regenerate said organic extractant solution; (g) recycling the regenerated organic extractant solution to step e; and (h) recovering tungsten values from the aqueous stripping solution, whereby the tungsten recovered contains less than 1 mole percent contaminating boron.
Claim 2
Dependent Claim 200 words
A process for recovering tungsten substantially free of contaminating boron from aqueous media containing tungsten and boron comprising the steps of: (a) adjusting the pH of said aqueous medium to a value below about pH 8; (b) contacting the pH-adjusted aqueous medium with an ion exchange resin to load the resin with tungsten and boron values from said aqueous medium; (c) eluting the loaded resin with an aqueous eluant solution to selectively recover a portion of the tungsten from said loaded resin; (d) adjusting the pH of the tungsten-containing aqueous eluate solution to a value below about pH 3; (e) contacting the pH-adjusted aqueous eluate solution with an organic extractant solution comprising o-mercaptobenzoic acid, a quaternary alkylammonium salt, and an inert organic solvent to transfer a portion of the tungsten values to the organic extractant solution; (f) contacting the tungsten-containing organic extractant solution with an aqueous stripping solution to transfer a portion of the tungsten values to said aqueous stripping solution and to regenerate said organic extractant solution; (g) recycling the regenerated organic extractant solution to step e; and (h) recovering tungsten values from the aqueous stripping solution, whereby the tungsten recovered contains less than 1 mole percent contaminating boron.
Claim 3
Dependent Claim 37 words
The process in accordance with claim 1 wherein said o-mercaptobenzoic acid is present in said organic extractant solution in a molar amount of from 2 to 20 times that of said tungsten in said aqueous eluate solution.
Claim 4
Dependent Claim 62 words
The process in accordance with claim 1 wherein said quaternary alkylammonium salt comprises a compound of the formula R 1 R 2 R 3 (CH 3 )N + X - where R 1 , R 2 , and R 3 are selected from the group consisting of C 8 to C 10 straight chain hydrocarbon groups and X is bromide or chloride.
Claim 5
Dependent Claim 16 words
The process in accordance with claim 3 wherein said quaternary alkylammonium salt comprises methyl tricaprylylammonium chloride.
Claim 6
Dependent Claim 22 words
The process in accordance with claim 3 wherein said inert organic solvent is selected from the group consisting of ≧C 7 hydrocarbons.
Claim 7
Dependent Claim 21 words
The process in accordance with claim 5 wherein said inert organic solvent further includes a C 8 to C 12 alcohol.
Claim 8
Dependent Claim 15 words
The process in accordance with claim 4 wherein said aqueous stripping solution comprises sodium hydroxide.
Claim 9
Dependent Claim 215 words
A process for recovering tungsten substantially free of contaminating boron from aqueous media containing tungsten and boron comprising the steps of: (a) adjusting the pH of said aqueous medium to a value below about pH 8; (b) contacting the pH-adjusted aqueous medium with an ion exchange resin comprising a copolymer of 8-hydroxyquinoline, ethylenediamine, resorcinol, and formaldehyde to load said resin with tungsten and boron values from said aqueous medium; (c) eluting the loaded resin with an aqueous eluant solution to selectively recover a portion of the tungsten from said loaded resin; (d) adjusting the pH of the tungsten-containing aqueous eluate solution to a value below about pH 3; (e) contacting the pH-adjusted aqueous eluate solution with an organic extractant solution comprising o-mercaptobenzoic acid, a quaternary alkylammonium salt, and an inert organic solvent to transfer a portion of the tungsten values to the organic extractant solution; (f) contacting the tungsten-containing organic extractant solution with an aqueous stripping solution of a base to transfer a portion of the tungsten values to said aqueous stripping solution and to regenerate said organic extractant solution; (g) recycling the regenerated organic extractant solution to step e; and (h) recovering tungsten values from the aqueous stripping solution, whereby the tungsten recovered by said process contains less than 1 mole percent contaminating boron.
Claim 10
Dependent Claim 215 words
A process for recovering tungsten substantially free of contaminating boron from aqueous media containing tungsten and boron comprising the steps of: (a) adjusting the pH of said aqueous medium to a value below about pH 8; (b) contacting the pH-adjusted aqueous medium with an ion exchange resin comprising a copolymer of 8-hydroxyquinoline, ethylenediamine, resorcinol, and formaldehyde to load said resin with tungsten and boron values from said aqueous medium; (c) eluting the loaded resin with an aqueous eluant solution to selectively recover a portion of the tungsten from said loaded resin; (d) adjusting the pH of the tungsten-containing aqueous eluate solution to a value below about pH 3; (e) contacting the pH-adjusted aqueous eluate solution with an organic extractant solution comprising o-mercaptobenzoic acid, a quaternary alkylammonium salt, and an inert organic solvent to transfer a portion of the tungsten values to the organic extractant solution; (f) contacting the tungsten-containing organic extractant solution with an aqueous stripping solution of a base to transfer a portion of the tungsten values to said aqueous stripping solution and to regenerate said organic extractant solution; (g) recycling the regenerated organic extractant solution to step e; and (h) recovering tungsten values from the aqueous stripping solution, whereby the tungsten recovered by said process contains less than 1 mole percent contaminating boron.
Claim 11
Dependent Claim 37 words
The process in accordance with claim 8 wherein said o-mercaptobenzoic acid is present in said organic extractant solution in a molar amount of from 2 to 20 times that of said tungsten in said aqueous eluate solution.
Claim 12
Dependent Claim 63 words
The process in accordance with claim 8 wherein said quaternary alkylammonium salt comprises a compound of the formula R 1 R 2 R 3 (CH 3 )N + X - where R 1 , R 2 , and R 3 are selected from the group consisting of C 8 to C 10 straight chain hydrocarbon groups and X - is bromide or chloride.
Claim 13
Dependent Claim 16 words
The process in accordance with claim 10 wherein said quaternary alkylammonium salt is methyl tricaprylylammonium chloride.
Claim 14
Dependent Claim 32 words
The process in accordance with claim 10 wherein said inert organic solvent comprises at least 80 volume percent ≧C 7 hydrocarbons with the balance comprising a C 8 to C 12 alcohol.
Claim 15
Dependent Claim 20 words
The process in accordance with claim 1 or claim 8 wherein said aqueous medium containing tungsten comprises Searles Lake brine.

References Cited (Backward Citations)

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USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1984-08-31 1985-03-02 1985-09-01 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1988-08-31 1989-03-02 1989-09-01 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1992-08-31 1993-03-02 1993-09-01 $7700.00 Window Closed / Lapsed

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