IP Library Patent Application 17876517
Patent Application
App. No. 17/876,517

RECOVERING URANIUM FROM A URANYL NITRATE SOLUTION

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Quick Facts
Patent No.
US None
App. No.
17/876,517
Abstract

A useful metal may be recovered from a solution of a nitrate salt of a metal cation or a metal oxycation, by adding the solution of the nitrate salt to a formation column having an inlet and an outlet nozzle, the solution of the nitrate salt being added in a dropwise fashion through the inlet. The formation column contains a recirculating solution containing a base selected from the group consisting of ammonia, ammonium hydroxide, an alkali metal hydroxide, and an alkaline earth metal hydroxide. The nitrate salt reacts with the base in the recirculating solution to produce a metal oxide salt or a metal hydroxide salt as a precipitate. The precipitate and the recirculating solution exit the formation column through the outlet nozzle and are captured the precipitate in a basket beneath the formation column while recovering the recirculating solution in a catch tank under the basket. The recovered recirculating solution is pumped from the catch tank to the formation column. The nitrate salt of the metal cation may be a nitrate salt of a radioactive metal cation, e.g., uranium or a uranyl cation.

Claims (66)

1 . A method of recovering a useful metal from a solution of a nitrate salt of a metal cation or a metal oxycation, comprising:

adding the solution of the nitrate salt to a formation column having an inlet and an outlet nozzle, the solution of the nitrate salt being added in a dropwise fashion through the inlet,

wherein the formation column contains a recirculating solution containing a base selected from the group consisting of ammonia, ammonium hydroxide, an alkali metal hydroxide, and an alkaline earth metal hydroxide;

allowing the nitrate salt in the solution to react with the base in the recirculating solution to produce a metal oxide salt or a metal hydroxide salt as a precipitate;

allowing the precipitate and the recirculating solution to exit the formation column through the outlet nozzle;

capturing the precipitate in a basket beneath the formation column while recovering the recirculating solution in a catch tank under the basket; and

pumping the recovered recirculating solution from the catch tank to the formation column.

2 . The method of claim 1 , wherein the nitrate salt is a salt of a cation or an oxycation of a main group metal, a transition metal, a lanthanide metal, or an actinide metal.

3 . The method of claim 1 , wherein the nitrate salt is uranyl nitrate, thorium nitrate, or plutonium nitrate.

4 . The method of claim 3 , wherein:

the nitrate salt is uranyl nitrate,

the base is ammonia or ammonium hydroxide, and

the precipitate is ammonium diuranate.

5 . The method of claim 4 , wherein the base is ammonium hydroxide.

6 . The method of claim 3 , wherein the nitrate salt is uranyl nitrate, the base is the alkali metal hydroxide, and the precipitate is an alkali metal diuranate.

7 . The method of claim 1 , further comprising:

washing the precipitate with an aqueous wash solution; and

drying the washed precipitate;

wherein the precipitate is kept in the basket during the washing and drying steps.

8 . The method of claim 7 , further comprising:

transporting the basket containing the captured precipitate from beneath the formation column into an oxidizing furnace.

heating the basket containing the captured precipitate in the oxidizing furnace to convert the precipitate into a metal oxide.

9 . The method of claim 8 , wherein:

the nitrate salt is uranyl nitrate,

the base is ammonia or ammonium hydroxide,

the precipitate is ammonium diuranate, and

the metal oxide is UO 2 , U 2 O 5 , UO 3 , U 3 O 8 , UO 2 O 2 , or a mixture thereof.

10 . The method of claim 1 , wherein the nitrate salt is iron(III) nitrate.

11 . The method of claim 10 , wherein:

the base is ammonium hydroxide, and

the precipitate is iron(III) hydroxide.

12 . The method of claim 1 , wherein the nitrate salt is yttrium(III) nitrate or cerium(III) nitrate.

13 . The method of claim 12 , wherein:

the base is ammonium hydroxide, and

the precipitate is yttrium(III) hydroxide or cerium(III) hydroxide.

14 . A system for recovering a useful metal from a solution of a nitrate salt of a metal cation or a metal oxycation, comprising:

a formation column having an inlet and an outlet nozzle, wherein the inlet is configured to admit the nitrate salt solution to the formation column in a dropwise fashion;

a basket under the outlet nozzle;

a catch tank under the basket; and

a recirculation system comprising a first pump and a flow path between the catch tank and the formation column, wherein:

the first pump is configured to pump a recirculating solution containing a base from the catch tank to the formation column; and

the catch tank is configured to receive the recirculating solution from the formation column;

wherein:

the formation column is configured to allow the base in the recirculating solution to react with the nitrate solution to produce a metal oxide salt as a precipitate;

the outlet nozzle is configured to allow the recirculating solution and the precipitate to exit the formation column; and

the basket is configured to capture the precipitate while allowing the recirculating solution to flow into the catch tank.

15 . The method of claim 14 , wherein the nitrate salt is uranyl nitrate, thorium nitrate, or plutonium nitrate.

16 . The method of claim 15 , wherein the nitrate salt is uranyl nitrate, the base is ammonia or ammonium hydroxide, and the precipitate is ammonium diuranate.

17 . The system of claim 14 , further comprising:

a wash station;

a wash solution outlet;

a wash tank below the wash solution outlet;

a second pump; and

a means for transporting the basket with the captured precipitate from under the outlet nozzle to the wash station;

wherein:

the second pump is configured to pump a wash solution from the wash tank to the wash solution outlet to produce a stream of wash solution; and

the means for transporting is configured to position the basket under the wash solution outlet so that the captured precipitate is washed by the stream of wash solution.

18 . The system of claim 14 , further comprising:

an oxidizing furnace; and

a means for transporting the basket with the washed precipitate from the wash station into the oxidizing furnace;

wherein the oxidizing furnace is configured to convert the precipitate into a metal oxide.

19 . The system of claim 18 , wherein:

the nitrate salt is uranyl nitrate,

the base is ammonia or ammonium hydroxide,

the precipitate is ammonium diuranate, and

the oxidizing furnace is configured to convert the precipitate into a uranium oxide.

Assignments (5)
RELEASE OF SECURITY INTEREST Recorded Feb 13, 2026
From: LIVE OAK BANKING COMPANY
To: X-ENERGY
Reel/Frame 073783/0139 →
SECURITY INTEREST Recorded May 12, 2025
From: X-ENERGY, LLC
To: LIVE OAK BANKING COMPANY
Reel/Frame 071081/0865 →
RELEASE OF INTELLECTUAL PROPERTY SECURITY INTEREST, RECORDED AT REEL/FRAME 068722/0427 Recorded Oct 11, 2024
From: AMAZON.COM NV INVESTMENT HOLDINGS, LLC
To: X-ENERGY, LLC
Reel/Frame 069717/0581 →
SECURITY INTEREST Recorded Sep 27, 2024
From: X-ENERGY, LLC
To: AMAZON.COM NV INVESTMENT HOLDINGS LLC
Reel/Frame 068722/0427 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Oct 27, 2022
From: TILTON, ALEX; LINNEEN, NICHOLAS
To: X-ENERGY, LLC
Reel/Frame 061565/0759 →