Hydrometallurgical treatment process for extracting constituent metal values from ferro-nickel

Claim 2

A hydrometallurgical treatment process for extracting constituent metal values from ferro-nickel containing cobalt, comprising the following steps: a. treating said ferro-nickel with chlorine in an aqueous medium and filtering the resultant matter; b. oxidising said filtrate; c. removing the iron contained in said oxidised filtrate by liquid/liguid extraction using an organic extractant (i) containing tributyl phosphate and regenerating said organic extractant (i) using an aqueous stripping solution (ii) thus yielding a pure aqueous solution of ferric chloride; and d. removing the cobalt contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (iii) containing a tertiary amine and regenerating said organic extractant (iii) using an aqueous stripping solution (iv) thus yielding a pure aqueous solution of cobalt cloride, the chloride, oxidised filtrate comprising a solution of nickel chloride.

Claim 3

The hydrometallurgical treatment process as claimed in claim 1, and further comprising: f. treating at least one of said solutions of ferric chloride, cobalt chloride, and nickel chloride to obtain the corresponding metal in elemental or other valuable form.

Claim 4

The hydrometallurgical treatment process as claimed in claim 2, wherein said treatment step (f) comprises an electrolysis treatment.

Claim 5

The hydrometallurgical treatment process as claimed in claim 3, wherein the chlorine liberated in said electrolysis is recycled to the treatment step (a).

Claim 6

The hydrometallurgical treatment process as claimed in claim 3, wherein said solution of ferric chloride is subjected to a first electrolysis to convert at least part of said ferric chloride to ferrous chloride, and subsequently to a second electrolysis yielding metallic iron.

Claim 7

The hydrometallurgical treatment process as claimed in claim 3, wherein each solution subjected to electrolysis has a pH of from 3 to 4.

Claim 8

The hydrometallurgical treatment process as claimed in claim 1, wherein said treatment step (a) is conducted at a temperature of from 70° to 110° C, the quantity of chlorine used being from 1.0 to 1.1 times the stoichiometric amount required.

Claim 9

The hydrometallurgical treatment process claimed in claim 1, wherein said oxidation step (b) also includes acidification of the oxidised filtrate to an acidity of 0.1 to 0.5N.

Claim 10

The hydrometallurgical treatment process as claimed in claim 1, wherein said removal step (c) of said iron comprises the following stages in succession: 1. contacting said oxidised filtrate from the oxidation step (b) with said organic extractant (i); 2. concentrating the extracted filtrate resulting from said contacting step (1); 3. contacting said concentrated extracted filtrate from said concentration step (2) with said organic extractant (i) resulting from said contacting step (1);

Claim 11

regenerating said organic extractant (i) resulting from said contacting step (3) using said aqueous stripping solution (ii) comprising water or acidified water; 5. contacting said concentrated extracted filtrate from said contacting step (3) with said regenerated organic extractant (i) from said regeneration step (4); and 6. recycling said organic extractant (i) to the contacting step (1).

Claim 12

regenerating said organic extractant (i) resulting from said contacting step (3) using said aqueous stripping solution (ii) comprising water or acidified water; 5. contacting said concentrated extracted filtrate from said contacting step (3) with said regenerated organic extractant (i) from said regeneration step (4); and 6. recycling said organic extractant (i) to the contacting step (1).

Claim 13

The hydrometallurgical treatment process as claimed in claim 1, wherein said oxidised filtrate after removal of said iron in step (c) contains at least 5 moles/liter of chloride ions.

Claim 14

The hydrometallurigical treatment process as claimed in claim 1 wherein said tertiary amine contained in said organic extractant (iii) is triisooctylamine.

Claim 15

A hydrometallurgical treatment process for extracting constituent metal values from ferro-nickel containing cobalt and chromium, comprising the following steps: a. treating said ferro-nickel with chlorine in an aqueous medium and filtering the resultant matter; b. oxidising said filtrate; c. removing the iron contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (i) containing tributyl phosphate and regenerating said organic extractant (i) using an aqueous stripping solution (ii) thus yielding a pure aqueous of ferric chloride; d. removing the cobalt contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (iii) containing a tertiary amine and regenerating said organic extractant (iii) using an aqueous stripping solution (iv) thus yielding a pure aqueous solution of cobalt chloride; and e. removing the chromium contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (v) containing an alkylphosphoric acid and regenerating said organic extractant (v) using an aqueous stripping solution (vi) thus yielding a pure aqueous solution of chromium chloride, the resultant oxidised filtrate comprising a solution of nickel chloride.

Claim 16

A hydrometallurgical treatment process for extracting constituent metal values from ferro-nickel containing cobalt and chromium, comprising the following steps: a. treating said ferro-nickel with chlorine in an aqueous medium and filtering the resultant matter; b. oxidising said filtrate; c. removing the iron contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (i) containing tributyl phosphate and regenerating said organic extractant (i) using an aqueous stripping solution (ii) thus yielding a pure aqueous of ferric chloride; d. removing the cobalt contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (iii) containing a tertiary amine and regenerating said organic extractant (iii) using an aqueous stripping solution (iv) thus yielding a pure aqueous solution of cobalt chloride; and e. removing the chromium contained in said oxidised filtrate by liquid/liquid extraction using an organic extractant (v) containing an alkylphosphoric acid and regenerating said organic extractant (v) using an aqueous stripping solution (vi) thus yielding a pure aqueous solution of chromium chloride, the resultant oxidised filtrate comprising a solution of nickel chloride.

Claim 17

The hydrometallurgical treatment process as claimed in claim 12, and further comprising: f. treating at least one of said solutions of ferric chloride, cobalt chloride, chromium chloride and nickel chloride to obtain the corresponding metal in elemental or other valuable form.

Claim 18

The hydrometallurgical treatment process as claimed in claim 13, wherein said treatment step (f) comprises an electrolysis treatment.

Claim 19

The hydrometallurgical treatment process as claimed in claim 14, wherein the chlorine liberated in said electrolysis is recycled to the treatment step (a).

Claim 20

The hydrometallurgical treatment process as claimed in claim 14, wherein said solution of ferric chloride is subjected to a first electrolysis to convert at least part of said ferric chloride to ferrous chloride, and subsequently to a second electrolysis yielding metallic iron.

Claim 21

The hydrometallurgical treatment process as claimed in claim 14, wherein each solution subjected to electrolysis has a pH of from 3 to 4.

Claim 22

The hydrometallurgical treatment process as claimed in claim 14, wherein said oxidised filtrate resulting from said removal step (d) contains more than 5 parts per million of chromium and wherein said removal step (c) of said chromium is performed prior to said electrolytic treatment (f) of the nickel chloride solution.

Claim 23

The hydrometallurgical treatment process as claimed in claim 12, wherein said removal step (e) of said chromium comprises the following stages: 1. contacting said oxidised filtrate with said organic extractant (v); 2. washing said organic extractant (v) with acidified water; 3. stripping said chromium contained in said organic extractant (v) with said aqueous stripping solution (vi) comprising concentrated hydrochloric acid;

Claim 24

treating said organic extractant (v) with a basic agent; and 5. contacting said organic extractant (v) with a solution of nickel chloride.

Claim 25

treating said organic extractant (v) with a basic agent; and 5. contacting said organic extractant (v) with a solution of nickel chloride.

Claim 26

The hydrometallurgical treatment process as claimed in claim 19, wherein said acidified water used for said washing of said organic extractant (v) has an acidity of from 0.1 to 1 N.

Claim 27

The hydrometallurgical treatment process as claimed in claim 12, wherein said treatment step (a) is conducted at a temperature of from 70° to 110° C, the quantity of chlorine used being from 1.0 to 1.1 times the stoichiometric amount required.

Claim 28

The hydrometallurgical treatment process as claimed in claim 12, wherein at least two-thirds of said alkylphosphoric acid contained in the organic extractant (v) is in the form of its nickel salt.