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US4233272A Expired / Lapsed US ⏱️ 0.0 years remaining

Process for selective separation of uranium from solutions by means of an ion exchanger

Assignee: Uranerzbergbau GmbH
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Filing: 1977-06-14
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Granted: 1980-11-11
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Expires: 1997-06-14
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Abstract

Abstract A process for selectively removing tetravalent and/or hexavalent uranium ions from a solution by using a chelate-forming cation exchanger. The solution may be prepared by contacting uranium bearing ore with either an acid or a dilute carbonate or bicarbonate solution. To facilitate removal of the uranium ions, the solution may have a pH value greater than 1.0 and a redox potential of from -50 to +250 mV.

Inventors

  • 👤 Nahit Eresen
  • 👤 Klaus Schroer
  • 👤 Hans J. Becker

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-10-27 15:21
CPC Classifications
C; C22; C22B; C22B60/00; C22B60/02; C22B60/0204; C22B60/0217; C22B60/0252; C22B60/0265; C22B3/00; C22B3/20; C22B3/42; Y; Y02; Y02P; Y02P10/00; Y02P10/20

Claims Analysis

Total Claims: 10
Claim 1
Independent Claim 73 words
A process for obtaining uranium from an ore containing uranium and arsenic comprising: (a) contacting the ore with an acid under oxidizing conditions to thereby form a pregnant liquor containing uranium and arsenate; (b) contacting the pregnant liquor with hydrogen sulfide to precipitate arsenic sulfide; (c) in the absence of an oxidizing step, contacting the hydrogen sulfide treated liquor with a chelate-forming cation exchanger; and (d) recovering uranium from the chelate-forming cation exchanger.
Claim 2
Dependent Claim 73 words
A process for obtaining uranium from an ore containing uranium and arsenic comprising: (a) contacting the ore with an acid under oxidizing conditions to thereby form a pregnant liquor containing uranium and arsenate; (b) contacting the pregnant liquor with hydrogen sulfide to precipitate arsenic sulfide; (c) in the absence of an oxidizing step, contacting the hydrogen sulfide treated liquor with a chelate-forming cation exchanger; and (d) recovering uranium from the chelate-forming cation exchanger.
Claim 3
Dependent Claim 25 words
The process of claim 1 wherein the liquor has a pH value greater than 1.0 and a redox potential of from -50 to 250 mV.
Claim 4
Dependent Claim 30 words
The process of claim 18 wherein the arsenic sulfide is precipitated at a pressure of from 1 to 4 bar and at a temperature of approximately 50° to 100° C.
Claim 5
Dependent Claim 31 words
The process of claim 3 wherein the uranium is recovered from the chelate-forming cation exchanger by eluting the exchanger with 5-15 percent sulfuric acid and precipitating the uranium from the eluate.
Claim 6
Dependent Claim 89 words
A process for obtaining uranium from an ore containing uranium and a material selected from the group consisting of arsenic, copper, molybdenum and lead comprising: (a) contacting the ore with an acid under oxidizing conditions to thereby form a pregnant liquor containing uranium and the material; (b) contacting the pregnant liquor with hydrogen sulfide to precipitate a sulfide of the material; (c) in the absence of an oxidizing step, contacting the hydrogen sulfide treated liquor with a chelate-forming cation exchanger; and (d) recovering uranium from the chelate-forming cation exchanger.
Claim 7
Dependent Claim 89 words
A process for obtaining uranium from an ore containing uranium and a material selected from the group consisting of arsenic, copper, molybdenum and lead comprising: (a) contacting the ore with an acid under oxidizing conditions to thereby form a pregnant liquor containing uranium and the material; (b) contacting the pregnant liquor with hydrogen sulfide to precipitate a sulfide of the material; (c) in the absence of an oxidizing step, contacting the hydrogen sulfide treated liquor with a chelate-forming cation exchanger; and (d) recovering uranium from the chelate-forming cation exchanger.
Claim 8
Dependent Claim 25 words
The process of claim 1 wherein the liquor has a pH value greater than 1.0 and a redox potential of from -50 to 250 mV.
Claim 9
Dependent Claim 32 words
The process of claim 2 wherein the sulfide of the material is precipitated at a pressure of from 1 to 4 bar and at a temperature of approximately 50° to 100° C.
Claim 10
Dependent Claim 31 words
The process of claim 3 wherein the uranium is recovered from the chelate-forming cation exchanger by eluting the exchanger with 5-15 percent sulfuric acid and precipitating the uranium from the eluate.

References Cited (Backward Citations)

US3268288A Cited
GB1115797A Cited
US3953568A Cited
US3880980A Cited
US4002716A Cited
US3998924A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-11-11 1984-05-12 1984-11-11 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-11-11 1988-05-12 1988-11-11 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-11-11 1992-05-12 1992-11-11 $7700.00 Window Closed / Lapsed

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