Extraction of uranium from wet-process phosphoric acid

1. A process for the extraction of uranium compounds from wet-process phosphoric acid (WPA), the process comprising:

lowering iron content of the WPA to produce a lowered iron WPA;

adding a reducing agent to the lowered iron WPA for reducing valency of any remaining iron in the lowered iron WPA to produce a reduced iron valency WPA; and

extracting uranium compounds from the reduced iron valency WPA.

2. The process of claim 1 , further comprising:

separating from the lowered iron WPA a side stream having a greater concentration of the uranium compounds than the WPA by passing the lowered iron WPA through a filter membrane to produce a clean WPA permeate and a retentate as the side stream, the retentate comprising a greater concentration of the uranium compounds than the concentration of uranium in the permeate.

3. The process of claim 2 , wherein the filter membrane is selected from an ultra-filtration or a nano-filtration membrane or combination thereof and comprising a pore size in the range of from 10 to 1,000 Å.

4. The process of claim 1 , wherein lowering iron content of the WPA comprises precipitating the iron as an iron ammonium phosphate.

5. The process of claim 4 , wherein precipitating the iron as an iron ammonium phosphate compound comprises adding ammonia, forming a precipitate, and separating the precipitate from the WPA.

6. The process of claim 1 , wherein reducing valency of iron in the WPA comprises reducing ferric iron to ferrous iron.

7. The process of claim 6 , wherein reducing the ferric iron to ferrous iron comprises contacting the WPA with a compound selected from one or more of the group consisting of: a ferro-phosphorous compound, a ferro-silicon compound, and metallic iron.

8. A process for extracting uranium species from wet-process phosphoric acid (WPA), the process comprising:

(a) decreasing the concentration of dissolved iron species in the WPA relative to the concentration of uranium species in the WPA to produce a decreased iron content WPA having uranium species therein;

(b) subjecting the decreased iron content WPA to a reduction step, wherein the valency of dissolved iron species remaining in the decreased iron content WPA is reduced; and

(c) extracting the uranium species from the decreased iron content WPA subsequent to the reduction step.

9. The process of claim 8 , further comprising:

separating from the decreased iron content WPA a side stream having a greater concentration of the uranium species than the WPA by passing the decreased iron content WPA through a filter membrane to produce a clean WPA permeate and a retentate as the side stream, the retentate comprising a greater concentration of the uranium species than the concentration of uranium in the permeate.

10. The process of claim 9 , wherein the filter membrane is selected from an ultra-filtration or a nano-filtration membrane or combination thereof and comprising a pore size in the range of from 10 to 1,000 Å.

11. The process of claim 8 , wherein decreasing the concentration of dissolved iron species in the WPA relative to the concentration of uranium species in the WPA comprises precipitating dissolved iron species as iron ammonium phosphate.

12. The process of claim 11 , wherein precipitating dissolved iron species as iron ammonium phosphate comprises adding ammonia, forming a precipitate, and separating the precipitate from the WPA.

13. The process of claim 8 , wherein the reduction step comprises reducing ferric iron to ferrous iron.

14. The process of claim 13 , wherein reducing the ferric iron to ferrous iron comprises contacting the WPA with a compound selected from the group consisting of: a ferro-phosphorous compound, a ferro-silicon compound, metallic iron, and a combination thereof.

15. A process for the extraction of uranium compounds from wet-process phosphoric acid (WPA), the process comprising:

(a) receiving a stream of raw WPA comprising uranium species, dissolved iron species, and suspended solids;

(b) passing the stream of raw WPA through a clarifier to remove suspended solids by flocculation, thereby creating a clarified WPA stream;

(c) filtering the clarified WPA stream to produce a retentate stream and a permeate stream, wherein the concentration of uranium species in the retentate stream is greater that the concentration of uranium species in the raw WPA;

(d) separating the permeate stream from the retentate stream;

(e) precipitating dissolved iron species from the retentate stream as iron ammonium phosphate by reacting the retentate stream with ammonia to form a lowered iron content retentate and a precipitant;

(f) removing the precipitant from the lowered iron content rententate by centrifugation;

(g) transferring the lowered iron content retentate to a reduction stage after centrifugation, wherein the lowered iron content retentate is treated to reduce the valency of any non-precipitated ferric iron in the lowered iron content retentate;

(h) lowering the concentration of uranium species in the lowered iron content retentate after the reduction stage by collecting uranium species in the lowered iron content retentate;

(i) forming a uranyl solution from the collected uranium species; and

(j) precipitating uranium oxide from the uranyl solution.

16. The process of claim 15 , wherein collecting uranium species comprises passing the lowered iron content retentate over a chelating ion exchange resin, wherein uranium species bind to the chelating ion exchange resin.

17. The process of claim 16 , wherein forming a uranyl solution comprises eluting with ammonium carbonate solution to form uranyl carbonate.

18. The process of claim 15 , wherein collecting uranium species comprises oxidizing the lowered iron content retentate after the reduction stage and subsequently extracting uranium via solvent extraction.

19. The process of claim 18 , wherein forming a uranyl solution comprises mixing a solvent used in solvent extraction with ammonium carbonate solution to form uranyl carbonate.