Method for preparing a high-purity hydrated nickel sulphate

1. A method of recovering NiSO 4 .6H 2 O crystals from a nickel rich organic phase, the method including:

contacting a nickel rich organic phase with an aqueous strip solution of sufficient H 2 SO 4 concentration to extract nickel from the organic phase and of sufficient Ni 2+ concentration to precipitate NiSO 4 .6H 2 O crystals and form a nickel lean organic phase.

2. The method of claim 1 , further including separating the NiSO 4 .6H 2 O crystals from the nickel lean organic phase.

3. The method of claim 1 , wherein the strip solution has a H 2 SO 4 concentration of 10-300 g/L.

4. The method of claim 1 , wherein the nickel rich organic phase includes a coordination complex of nickel and an organic extractant, wherein the organic extractant dissociates from the nickel in the presence of a sufficient concentration of H + ions.

5. The method of claim 4 , wherein the organic extractant is selected from the group consisting of: organophosphorous acids, chelating oximes or hydroxyoximes, carboxylic acids, and high molecular weight amines.

6. The method of claim 4 , wherein the organic extractant is a branched carboxylic acid that has the structure:

wherein R 1 and R 2 are branched or straight chain unsubstituted alkyl groups, and R 1 and R 2 together consist of from 5 to 13 carbon atoms.

7. The method of claim 1 , wherein the method includes:

a nickel solvent extraction step including contacting an aqueous acidic nickel sulphate containing solution with an organic phase including an organic extractant to selectively extract nickel sulphate from the aqueous solution into the organic phase to form a nickel sulphate lean aqueous raffinate and the nickel rich organic phase; and

separating the raffinate and the nickel rich organic phase;

wherein the organic extractant is one or more branched carboxylic acids.

8. The method of claim 7 , wherein the method includes:

cobalt extraction of the nickel sulphate containing solution prior to nickel solvent extraction, wherein the cobalt extraction step includes an organic extractant that selectively extracts cobalt over nickel into an organic phase to form a cobalt-rich nickel-lean extractant stream and a cobalt-lean nickel-rich raffinate.

9. The method of claim 7 , wherein the nickel sulphate containing solution is a pregnant leach solution derived from the low temperature pressure oxidation of a nickel sulphide concentrate.

10. The method of claim 7 , wherein the nickel sulphate containing solution is a pregnant leach solution derived from the low temperature pressure oxidation of nickel sulphide concentrate, the sulphide concentrate containing more than 10% nickel.

11. The method of claim 1 , wherein the method includes:

a nickel solvent extraction step including contacting an aqueous solution including nickel sulphate and one or more metal impurities with an organic phase, the organic phase including one or more branched carboxylic acid extractants to selectively facilitate the extraction of nickel sulphate from aqueous solution into the organic phase and form the nickel rich organic phase.

12. The method of claim 1 , wherein the method includes:

a nickel solvent extraction step including contacting an aqueous nickel sulphate containing solution with an organic phase including an organic extractant to form the nickel rich organic phase, wherein the aqueous nickel sulphate containing solution is a pregnant leach solution (PLS) that is a cobalt-lean nickel-rich raffinate.

13. The method of claim 1 , wherein the NiSO 4 .6H 2 O crystals include: 5 ppm or less Fe and/or 5 ppm or less Mn and/or 5 ppm or less Cu and/or 60 ppm or less Co and/or 10 ppm or less Zn.

14. The method of claim 1 , wherein the strip solution has a Ni 2+ concentration of 60 g/L or greater.

15. A method for producing nickel sulphate, the method including the steps of:

a) providing a source of nickel sulphide concentrate;

b) repulping the nickel sulphide of step (a) concentrate;

c) fine grinding the nickel sulphide concentrate from step (b) to a P 80 of 10 microns;

d) low temperature pressure oxidation (LTPOX) autoclaving of the nickel sulphide concentrate from step (c) to afford a pregnant leach solution (PLS), wherein the nickel sulphide concentrate contains more than 10% nickel;

e) neutralising the PLS of step (d) using one or more bases selected from the group including ammonium hydroxide, limestone, lime, calcrete, magnesia, magnesite and sodium hydroxide;

f) counter current decantation of the PLS from step (e) to separate solids from the slurry of the PLS;

g) neutralising the PLS from step (f) using one or more bases selected from the group including ammonium hydroxide, limestone, lime, calcrete, magnesia, magnesite and sodium hydroxide;

h) optionally clarifying the PLS from step (g);

i) extracting cobalt from the PLS of step (g) or step (h), wherein the cobalt extraction includes an organic extractant that selectively extracts cobalt over nickel into an organic phase to form a cobalt-rich nickel-lean extractant stream and a cobalt-lean nickel-rich raffinate;

j) extracting nickel from the cobalt-lean nickel-rich raffinate of step (i); wherein the nickel extraction includes contacting the cobalt-lean nickel-rich raffinate with an organic phase including an organic extractant to form a nickel-rich organic phase; and

k) direct crystallisation of the nickel-rich organic phase of step (j), wherein the direct crystallisation includes contacting the nickel-rich organic phase with an aqueous strip solution of sufficient H 2 SO 4 concentration to extract nickel from the organic phase and of sufficient Ni 2+ concentration to precipitate NiSO 4 .6H 2 O crystals and form a nickel-lean organic phase;

wherein the nickel sulphate is between 21 and 24% nickel and is in the form of nickel sulphate hexahydrate (NiSO 4 .6H 2 O).