Ion exchange recovery of uranium

Claim 2

A process for recovering soluble uranium with an ion exchange material from carbonate-containing water, comprising the combination and sequence of steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of ion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxyl, carbonate and bicarbonate ions, and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) treating the mass of ion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of a metal hydroxide and ammonium hydroxide to expel any carbonate contained therein; and (c) removing the retained ions comprising uranium from the ion exchange material by contacting said material with an acid and recovering the uranium.

Claim 3

The process of claim 1, wherein the ion exchange material expended by the uranium recovery is regenerated by contacting said expended exchange material with at least one alkali solution selected from the group consisting of hydroxides, carbonates and bicarbonates of a metal or ammonium.

Claim 4

The process of claim 2, wherein the alkali solution for regenerating the ion exchange material is a solution of an alkali metal hydroxide.

Claim 5

The process of claim 1, wherein the mass of ion exchange material having uranium ions retained thereon from contacting said carbonate-containing water, is washed with dilute ammonium hydroxide solution to displace the carbonate-containing water from about the exchange material.

Claim 6

The process of claim 1, wherein the acid for removing any retained ions comprising uranium is nitric acid.

Claim 7

The process of claim 1, wherein the metal hydroxide for treating the mass of ion exchange material is an alkali metal hydroxide.

Claim 8

A process for recovering soluble uranium with an ion exchange material from carbonate-containing water, comprising the combination and sequence of steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate ion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxide, carbonate and bicarbonate ions, and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of ion exchange material having the uranium ions retained thereon with water to displace the carbonate-containing water from about the exchange material; (c) treating the mass of ion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of an alkali metal hydroxide and ammonium hydroxide to expel any carbonate contained therein; (d) removing retained ions comprising uranium from the ion exchange material by contacting said material with a mineral acid and recovering the uranium; and (e) regenerating the ion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates and bicarbonates of an alkali metal and ammonium to thereby charge said exchange material with exchangeable ions.

Claim 9

A process for recovering soluble uranium with an ion exchange material from carbonate-containing water, comprising the combination and sequence of steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate ion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxide, carbonate and bicarbonate ions, and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of ion exchange material having the uranium ions retained thereon with water to displace the carbonate-containing water from about the exchange material; (c) treating the mass of ion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of an alkali metal hydroxide and ammonium hydroxide to expel any carbonate contained therein; (d) removing retained ions comprising uranium from the ion exchange material by contacting said material with a mineral acid and recovering the uranium; and (e) regenerating the ion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates and bicarbonates of an alkali metal and ammonium to thereby charge said exchange material with exchangeable ions.

Claim 10

The process of claim 7, wherein the water for washing the mass of ion exchange material having uranium ions retained thereon to displace the carbonate-containing water from about the exchange material comprises a solution of ammonium hydroxide.

Claim 11

The process of claim 7, wherein the mineral acid for removing any retained ions comprising uranium is nitric acid.

Claim 12

The process of claim 7, wherein the alkali solution for regenerating the expended ion exchange material is a solution of sodium hydroxide.

Claim 13

The process of claim 7, wherein the alkali solution for regenerating the expended ion exchange material is a solution of ammonium hydroxide.

Claim 14

The process of claim 7, wherein the mass of ion exchange material having had any retained ions comprising uranium removed therefrom by contact with a mineral acid, is washed with water to displace any mineral acid remaining thereabout.

Claim 15

The process of claim 7, wherein the solution of a hydroxide for treating the mass of ion exchange material comprises a solution of sodium hydroxide.

Claim 16

A process for recovering soluble uranium with an anion exchange material from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate anion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxyl, carbonate or bicarbonate ions, and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the carbonate-containing water from about the exchange material; (c) treating the mass of anion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of an alkali metal hydroxide and ammonium hydroxide to expel any carbonate contained therein; (d) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the solution of a hydroxide from about the exchange material; (e) removing retained ions comprising uranium from the anion exchange material by contacting said material with nitric acid and recovering the uranium; (f) washing the mass of anion exchange material having had the retained uranium ions removed therefrom with water to displace any nitric acid from about the exchange material; and (g) regenerating the anion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates, and bicarbonates of an alkali metal and ammonium to thereby charge said exchange material with exchangeable ions.

Claim 17

A process for recovering soluble uranium with an anion exchange material from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate anion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxyl, carbonate or bicarbonate ions, and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the carbonate-containing water from about the exchange material; (c) treating the mass of anion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of an alkali metal hydroxide and ammonium hydroxide to expel any carbonate contained therein; (d) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the solution of a hydroxide from about the exchange material; (e) removing retained ions comprising uranium from the anion exchange material by contacting said material with nitric acid and recovering the uranium; (f) washing the mass of anion exchange material having had the retained uranium ions removed therefrom with water to displace any nitric acid from about the exchange material; and (g) regenerating the anion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates, and bicarbonates of an alkali metal and ammonium to thereby charge said exchange material with exchangeable ions.

Claim 18

The process of claim 14, wherein the water for washing the mass of anion exchange material having uranium ions retained thereon to displace the carbonate-containing water from about the exchange material comprises a solution of ammonium hydroxide.

Claim 19

The process of claim 14, wherein the alkali solution for regenerating the expended ion exchange material is a solution of sodium hydroxide.

Claim 20

The process of claim 14, wherein the alkali solution for regenerating the expended ion exchange material is a solution of ammonium hydroxide.

Claim 21

The process of claim 14, wherein the alkali solution for regenerating the expended ion exchange material is a solution of sodium carbonate.

Claim 22

The process of claim 14, wherein the alkali solution for regenerating the expended ion exchange material is a solution of ammonium carbonate.

Claim 23

The process of claim 14, wherein the solution of a hydroxide for treating the mass of ion exchange material comprises a solution of sodium hydroxide.

Claim 24

A process for recovering soluble uranium with an anion exchange material from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate anion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxide, carbonate and bicarbonate ions and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of anion exchange material having the uranium ions retained thereon with a solution of ammonium hydroxide to displace the carbonate-containing water from about the exchange material; (c) treating the mass of particulate anion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of sodium hydroxide and ammonium hydroxide to expel any carbonate entrained within the mass of particulate exchange material; (d) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the basic solution from about the exchange material; (e) removing retained ions comprising uranium from the anion exchange material by contacting said exchange material with nitric acid and recovering the removed uranium from the resultant effluent; (f) washing the mass of anion exchange material having had the retained uranium ions removed therefrom with water to displace any nitric acid from about the exchange material; and (g) regenerating the mass of anion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates and bicarbonates of sodium and ammonium to thereby charge said anion exchange material with exchangeable ions.

Claim 25

A process for recovering soluble uranium with an anion exchange material from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble uranium therein with a mass of particulate anion exchange material charged with at least one exchangeable ion selected from the group consisting of hydroxide, carbonate and bicarbonate ions and thereby removing and retaining thereon uranium ions from said carbonate-containing water; (b) washing the mass of anion exchange material having the uranium ions retained thereon with a solution of ammonium hydroxide to displace the carbonate-containing water from about the exchange material; (c) treating the mass of particulate anion exchange material having the uranium ions retained thereon by passing therethrough a solution of a hydroxide selected from the group consisting of sodium hydroxide and ammonium hydroxide to expel any carbonate entrained within the mass of particulate exchange material; (d) washing the mass of anion exchange material having the uranium ions retained thereon with water to displace the basic solution from about the exchange material; (e) removing retained ions comprising uranium from the anion exchange material by contacting said exchange material with nitric acid and recovering the removed uranium from the resultant effluent; (f) washing the mass of anion exchange material having had the retained uranium ions removed therefrom with water to displace any nitric acid from about the exchange material; and (g) regenerating the mass of anion exchange material by contacting the ion exchange material expended by the uranium recovery with at least one alkali solution selected from the group consisting of hydroxides, carbonates and bicarbonates of sodium and ammonium to thereby charge said anion exchange material with exchangeable ions.

Claim 26

A process for recovering soluble uranium with an anion exchange resin from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble complex uranyl anions therein with a mass of particulate anion exchange resin charged with hydroxyl ions and thereby removing and retaining thereon complex uranyl anions from said carbonate-containing water; (b) washing the mass of anion exchange resin having the complex uranyl anions retained thereon with water to displace the carbonate-containing water from about the exchange resin; (c) treating the mass of particulate anion exchange resin having the complex uranyl anions retained thereon by passing therethrough a solution of sodium hydroxide to expel any carbonate entrained within the mass of particulate exchange resin; (d) washing the mass of anion exchange resin having the complex uranyl anion retained thereon with water to displace the sodium hydroxide solution from about the exchange resin; (e) removing any retained complex uranyl anions from the anion exchange resin by contacting said exchange resin with nitric acid and recovering the removed complex uranyl anions from the resultant effluent; (f) washing the mass of anion exchange resin having had the retained complex uranyl anions removed therefrom with water to displace any nitric acid from about the exchange resin; and, (g) regenerating the mass of anion exchange resin by contacting the anion exchange resin expended by the uranium recovery with a solution of sodium hydroxide to thereby charge said anion exchange resin with hydroxyl ions.

Claim 27

A process for recovering soluble uranium with an anion exchange resin from carbonate-containing water, comprising the steps of: (a) contacting carbonate-containing water having soluble complex uranyl anions therein with a mass of particulate anion exchange resin charged with hydroxyl ions and thereby removing and retaining thereon complex uranyl anions from said carbonate-containing water; (b) washing the mass of anion exchange resin having the complex uranyl anions retained thereon with water to displace the carbonate-containing water from about the exchange resin; (c) treating the mass of particulate anion exchange resin having the complex uranyl anions retained thereon by passing therethrough a solution of sodium hydroxide to expel any carbonate entrained within the mass of particulate exchange resin; (d) washing the mass of anion exchange resin having the complex uranyl anion retained thereon with water to displace the sodium hydroxide solution from about the exchange resin; (e) removing any retained complex uranyl anions from the anion exchange resin by contacting said exchange resin with nitric acid and recovering the removed complex uranyl anions from the resultant effluent; (f) washing the mass of anion exchange resin having had the retained complex uranyl anions removed therefrom with water to displace any nitric acid from about the exchange resin; and, (g) regenerating the mass of anion exchange resin by contacting the anion exchange resin expended by the uranium recovery with a solution of sodium hydroxide to thereby charge said anion exchange resin with hydroxyl ions.

Claim 28

The process of claim 22, wherein the soluble complex uranyl anions comprise uranium complexes with fluoride, hydroxide, and carbonate anions, and mixed complex ions thereof.