IP Library Patent Application 17291106
Patent Application
App. No. 17/291,106

PREPARATION OF TITANIUM DIOXIDE

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Quick Facts
Patent No.
US None
App. No.
17/291,106
Abstract

A method for the preparation of titanium dioxide, the method comprising the steps of subjecting a titanium containing leach residue to a concentrated sulfuric acid digest step; and in turn subjecting that residue to a leach in dilute sulfuric acid, whereby a black liquor is obtained and from which titanium dioxide is in turn obtained.

Claims (39)

1 . A method for the preparation of titanium dioxide, the method comprising the steps of:

(i) subjecting a titanium containing leach residue to a concentrated sulfuric acid digest step; and

(ii) in turn subjecting that residue to a leach in dilute sulfuric acid to obtain a black liquor from which titanium dioxide is in turn obtained,

wherein the leach residue is a residue from a hydrochloric leach of a titanomagnetite-type ore.

2 . The method of claim 1 , wherein the titanium dioxide is utilised in the preparation of a titanium dioxide pigment.

3 . The method of claim 1 , wherein the concentration of hydrochloric acid ranges between:

(i) about 15% to 32% (w/w); or

(ii) about 15% to 20% (w/w).

4 . The method of claim 1 , wherein a feedstock for the leach of the titanomagnetite-type ore is the product of a ferric leach.

5 . The method of claim 1 , a feedstock for the leach of the titanomagnetite-type ore is the product of a ferric leach, the ferric leach step having been conducted with ferric chloride.

6 . The method of claim 5 , wherein the concentration of ferric chloride ranges between:

(i) about 10 to 40% w/w;

(ii) about 25 to 35% w/w; or

(iii) about 28% w/w.

7 . The method of claim 1 , wherein the titanium containing leach residue has a P 80 of:

(i) ≤125 μm;

(ii) ≤45 μm; or

(iii) <40 μm.

8 . The method of claim 1 , wherein recovery of titanium into the black liquor is at least 98%.

9 . The method of claim 1 , wherein the digest step is conducted at a temperature of:

(i) greater than 175° C.; or

(ii) about 190° C.

10 . The method of claim 1 , wherein the digest step is conducted over a period of:

(i) between about 3 to 4 hours; or

(ii) about 3 hours.

11 . The method of claim 1 , wherein the mix of leach residue to concentrated sulfuric acid in the digest step is in the ratio of about 1:1.27 (g/g).

12 . The method of claim 1 , wherein at least 1.9 g of concentrated sulfuric acid is provided in the digest step (i) for every gram of TiO 2 in the titanium containing leach residue.

13 . The method of claim 1 , wherein the dilute sulfuric acid of the leach step (ii) is about 6% sulfuric acid.

14 . The method of claim 1 , wherein the leach step (ii) is conducted at about 60° C.

15 . The method of claim 1 , wherein the leach step (ii) is conducted for a period of about 15 hours.

16 . The method of claim 1 , wherein the leach step (ii) is conducted at about 20% solids.

17 . The method of claim 1 , wherein the black liquor is recovered from a slurry produced by the leach step (ii) by filtration, and the solids washed to recover titanium.

18 . The method of claim 1 , wherein the digest step (i):

(i) proceeds in an autothermic manner;

(ii) further comprises an initial dilution of the acid; or

(iii) further comprises an initial dilution of the acid to about 88-92% with water.

19 . (canceled)

20 . (canceled)

21 . The method of claim 1 , wherein the black liquor is passed to hydrolysis and calcination for the recovery of titanium dioxide.

Assignments (2)
CHANGE OF NAME Recorded Jan 31, 2023
From: TNG LIMITED
To: TIVAN LIMITED
Reel/Frame 062548/0749 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 17, 2021
From: CONNELLY, DAMIAN EDWARD GERARD
To: TNG LIMITED
Reel/Frame 057203/0789 →