Solvent extraction process

1. A process for extracting uranium from saline acidic uranium, chloride, iron (III) and sulphate containing solution having >5 g/L chloride, comprising:

a. contacting the solution with an organic phase containing a trialkylphosphine oxide (TAPO) as an extractant to form a uranium loaded organic phase;

b. scrubbing the uranium loaded organic phase with a scrubbing solution comprising a sulphuric acid based aqueous solution to remove any impurities and to form a scrubbed organic phase;

c. stripping uranium from the scrubbed organic phase with a concentrated sulphate solution having a sulphate concentration greater than IM to produce an aqueous uranium strip solution; and

d. precipitating a uranium product from the aqueous uranium strip solution.

2. The process of claim 1 wherein the trialkylphosphine oxide is a trioctylphosphine oxide.

3. The process of claim 1 wherein the organic phase includes a blend of at least two trialkylphosphine oxides.

4. The process of claim 1 wherein the organic phase additionally includes a substituted amine or its salt.

5. The process of claim 4 wherein the ratio of trialkylphosphine oxide to substituted amine or its salt is varied according to the level of impurities in the acidic uranium and chloride containing solution.

6. The process of claim 4 wherein the ratio of trialkylphosphine oxide to substituted amine or its salt is varied according to the salinity of the acidic uranium and chloride containing solution.

7. The process of claim 4 wherein at chloride concentrations above 5 g/l, the molar ratio of substituted amine or its salt to TAPO in the organic phase is a minimum of 90:10.

8. The process of claim 4 wherein at chloride concentrations above 10 g/l, the ratio of substituted amine or its salt to TAPO in the organic phase is at least 50:50.

9. The process of claim 1 wherein at chloride concentrations above 20 g/l, the organic phase contains no substituted amine or its salt.

10. The process of claim 1 , where the sulfuric acid based aqueous solution has an acid concentration from 0.1 M-1.0 M.

11. The process of claim 1 wherein the scrubbed organic is stripped using an ammonium sulfate solution.

12. The process of claim 11 , wherein the ammonium sulfate is solution has a concentration of up to saturation.

13. The process of claim 1 wherein the scrubbed organic is stripped using a sodium sulfate solution.

14. The process of claim 1 wherein the process is conducted at a temperature up to 50° C.

15. The process of claim 1 wherein the uranium product is an ammonium diuranate (ADU).

16. The process of claim 1 wherein the process is operated continuously.

17. A process for extracting uranium from an acidic saline uranium and iron (III) solution having >5 g/L chloride, comprising:

a. contacting the solution with an organic phase containing a trialkylphosphine oxide as an extractant to form a uranium loaded organic phase;

b. scrubbing the uranium loaded organic phase with a scrubbing solution comprising a sulphuric acid based aqueous solution to remove any impurities and to form a scrubbed organic phase;

c. stripping uranium from the scrubbed organic phase with a concentrated sulphate solution to produce an aqueous uranium strip solution; and

d. precipitating a uranium product from the aqueous uranium strip solution.

18. A process for extracting uranium from an acidic saline uranium and iron (III) containing solution comprising contacting the solution with an organic phase containing a trialkylphosphine oxide (TAPO) and a substituted amine or its salt as extractants, wherein the organic phase has a ratio of the TAPO to the substituted amine or substituted amine salt which is determined by the chloride concentration in the saline uranium containing solution.