Methods of making upgraded synthetic rutile

Patent metadata

Field	Value
Publication number	US-2026015691-A1
Application number	US-202318993819-A
Country	US
Kind code	A1
Filing date	Jul 12, 2023
Priority date	Jul 12, 2022
Publication date	Jan 15, 2026
Grant date	—

Abstract

A method of making upgraded synthetic rutile ( 100 ) can include binding ilmenite ultrafine particles together with a binder to form green pellets ( 110 ). Iron can be reduced in the green pellets by heating the green pellets to a reducing temperature under a reducing atmosphere ( 120 ). The ilmenite ultrafine particles within the green pellets can be at least partially sintered together by heating the green pellets at a sintering temperature to form at least partially sintered pellets ( 130 ). Iron can be removed from the at least partially sintered pellets by leaching to form upgraded synthetic rutile ( 140 ).

First claim

What is claimed is:

1 . A method of making upgraded synthetic rutile, comprising:
binding ilmenite ultrafine titanium-containing particles together with an optional binder to form green pellets; reducing iron in the green pellets by heating the green pellets to a reducing temperature under a reducing atmosphere; at least partially sintering together the ilmenite ultrafine titanium-containing particles within the green pellets by heating the green pellets at a sintering temperature to form at least partially sintered pellets; and removing iron from the at least partially sintered pellets by leaching to form upgraded synthetic rutile.

2 . The method of claim 1 , further comprising forming the ilmenite ultrafine titanium-containing particles by milling ilmenite ore.

3 . The method of claim 1 , wherein the ilmenite ultrafine titanium-containing particles have an average particle size from about 0.1 micrometer to about 50 micrometers.

4 . The method of claim 1 , wherein the ilmenite ultrafine titanium-containing particles include titanium dioxide in an amount from about 40 wt % to about 65 wt % and iron in an amount from about 15 wt % to about 31 wt %.

5 . The method of claim 1 , wherein the optional binder is present and is an organic binder.

6 . The method of claim 5 , wherein the organic binder comprises polyethylene, polypropylene, polyethylene glycol, polyvinylpyrrolidone, polyoxymethylene, polylactic acid, nylon, hyaluronate, cellulose, starches, or a combination thereof.

7 . The method of claim 5 , wherein binding the ilmenite ultrafine titanium-containing particles together comprises spraying a solution of the organic binder while tumbling the ultrafine ilmenite titanium-containing particles in a rotating vessel.

8 . The method of claim 7 , wherein the solution of the organic binder includes the organic binder dissolved in a solvent comprising ethanol, methanol, water, or a combination thereof.

9 . The method of claim 7 , wherein a concentration of organic binder in the solution is from about 0.1 wt % to about 5 wt %.

10 . The method of claim 5 , wherein the organic binder is vaporized or decomposed during the heating the green pellets to the reducing temperature.

11 . The method of claim 5 , wherein no carbon is added to the ilmenite ultrafine titanium-containing particles when forming the green pellets other than the organic binder.

12 . The method of claim 1 , wherein the green pellets have an average particle size from about 75 μm to about 1500 μm.

13 . The method of claim 1 , wherein the reducing temperature is from about 400° C. to about 1000° C.

14 . The method of claim 1 , wherein reducing the iron in the green pellets comprises holding the green pellets at the reducing temperature for a reducing time from about 0.1 hours to about 16 hours.

15 . The method of claim 1 , wherein the reducing atmosphere is hydrogen gas.

16 . The method of claim 1 , wherein the at least partially sintering is performed under the reducing atmosphere.

17 . The method of claim 1 , wherein the sintering temperature is greater than the reducing temperature.

18 . The method of claim 17 , wherein the green pellets are heated from the reducing temperature to the sintering temperature without cooling the green pellets below the reducing temperature in between.

19 . The method of claim 17 , wherein the green pellets are heated to the sintering temperature after letting the green pellets cool below the reducing temperature.

20 . The method of claim 1 , wherein the sintering temperature is from about 900° C. to about 1500° C.

21 . The method of claim 1 , wherein the at least partially sintering comprises holding the green pellets at the sintering temperature for a sintering time from about 10 minutes to about 2 hours.

22 . The method of claim 1 , wherein the at least partially sintering is partially sintering the ilmenite ultrafine titanium-containing particles so that at least some void space between the ilmenite ultrafine titanium-containing particles remains in the at least partially sintered pellets.

23 . The method of claim 1 , wherein leaching includes dissolving the iron with hydrochloric acid, sulfuric acid, or by aeration with ammonium chloride.

24 . The method of claim 23 , wherein hydrogen gas is produced during leaching, and wherein the method further comprises recycling the hydrogen gas to the reducing atmosphere used during reducing iron in a subsequent batch of green pellets.

25 . The method of claim 1 , further comprising recovering the iron that was removed by leaching.

26 . The method of claim 1 , further comprising pre-oxidizing iron(II) in the green pellets to iron(III) before the reducing.

27 . The method of claim 1 , wherein the upgraded synthetic rutile comprises titanium dioxide in an amount greater than 88 wt %.

28 . The method of claim 1 , wherein the upgraded synthetic rutile comprises rutile, anatase, or a combination thereof.

29 . The method of claim 1 , wherein the upgraded synthetic rutile has an average particle size from about 100 μm to about 1000 μm.

30 . The method of claim 1 , wherein the upgraded synthetic rutile has a porosity of 5 to 20% by volume.

31 . The method of claim 1 , further comprising using the upgraded synthetic rutile as a feedstock in a fluidized bed.

32 . The method of claim 31 , wherein the fluidized bed is used in a chloride process of purifying titanium dioxide.

33 . An upgraded synthetic titanium dioxide pellet, comprising a plurality of partially sintered together ultrafine particles, wherein the ultrafine particles have an average particle size from about 0.1 micrometer to about 10 micrometers, wherein void spaces are present between at least some of the partially sintered together ultrafine particles, and wherein the upgraded synthetic titanium dioxide pellet has a diameter from about 100 μm to about 1000 μm.

34 . The upgraded synthetic titanium dioxide pellet of claim 33 , wherein the upgraded synthetic titanium dioxide pellet comprises titanium dioxide in an amount greater than 88 wt %.

35 . The upgraded synthetic titanium dioxide pellet of claim 33 , wherein the upgraded synthetic titanium dioxide pellet has a porosity of 5-50%.

36 . The upgraded synthetic titanium dioxide pellet of claim 33 , wherein the upgraded synthetic titanium dioxide pellet is free of inorganic binder.

Assignees

• Univ Utah Res Found

Inventors

• Sun Pei
• Fang Zhigang Z
• Engstrom Nick

Classifications

• C22B34/125

  containing a sulfur ion as active agent · CPC title

• C22B34/1245

  containing a halogen ion as active agent · CPC title

• C22B3/04

  by leaching (C22B3/18 takes precedence) · CPC title

• C22B1/244

  organic · CPC title

• C22B1/2406

  pelletizing · CPC title