IP Library Granted Patent US 8,226,911
Granted Patent B2
US 8,226,911 · App. 12/584,699 · Granted Jul 24, 2012

Methods of producing titanium dioxide nanoparticles

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Quick Facts
Patent No.
US 8,226,911
App. No.
12/584,699
Granted
Jul 24, 2012
Kind
B2
Abstract

A method is provided for producing TiO 2 nanoparticles. The nanoparticles can be further processed by neutralization, calcination, and/or micronization. The TiO 2 nanoparticle size is controlled by controlling synthetic and process conditions. TiO 2 nanoparticles produced are of the anatase polymorph, of the rutile polymorph, or a mixture thereof, and have particle sizes in the range of from 10 nm to 100 nm.

Claims (24)

1. A method for manufacturing titanium dioxide crystalline powders, comprising:

thermally hydrolyzing an aqueous titanium oxychloride solution free of titanium dioxide nucleating agents, to form a resultant suspension;

neutralizing the resultant suspension to form a neutralized product;

filtering the neutralized product to form a filtered neutralized product; and

calcining the filtered neutralized product at a temperature of from 300° C. to 700° C., or 800° C. or higher, to form a calcined product.

2. The method of claim 1 , wherein the titanium oxychloride solution comprises from 0.687 to 2.5 moles of titanium ions per liter of solution.

3. The method of claim 2 , wherein the calcined product exhibits a specific surface area of from 50 m 2 /g to 300 m 2 /g.

4. The method of claim 2 , wherein the calcined product comprises more than 99% titanium dioxide of the anatase polymorph.

5. The method of claim 1 , wherein the titanium oxychloride solution comprises from 2.5 to 3.5 moles of titanium ions per liter of solution.

6. The method of claim 5 , wherein the calcined product exhibits a BET specific surface area of from 30 m 2 /g to 100 m 2 /g.

7. The method of claim 5 , wherein the calcined product comprises more than 99.5% by weight titanium dioxide of the rutile polymorph.

8. The method of claim 1 , wherein sulphate ions are added to the aqueous titanium oxychloride solution prior to the thermally hydrolyzing to form a resultant aqueous titanium oxychloride solution, and the calcined product comprises more than 50% by weight titanium dioxide of the anatase polymorph.

9. The method of claim 8 , wherein the sulphate ions are added in an amount to result in a concentration of sulphate ions in a range of from 0.01 mole to 1.0 mole per liter based on the volume of the resultant aqueous titanium oxychloride solution.

10. The method of claim 1 , wherein aluminum ions are added to the aqueous titanium oxychloride solution prior to the thermally hydrolyzing to form a resultant aqueous titanium oxychloride solution, and the calcined product comprises more than 50% by weight titanium dioxide of the rutile polymorph.

11. The method of claim 10 , wherein the aluminum ions are added in an amount to result in a concentration of aluminum ions in a range of from 0.045 mole to 0.15 mole per liter based on the volume of the resultant aqueous titanium oxychloride solution.

12. The method of claim 1 , wherein the thermally hydrolyzing is carried out at a temperature of from 95° C. to 105° C.

13. The method of claim 1 , wherein the thermally hydrolyzing is carried out at atmospheric pressure.

14. The method of claim 1 , wherein the thermally hydrolyzing is carried out for a time of from one hour to two hours.

15. The method of claim 1 , further comprising drying the filtered neutralized product at a temperature of from 80° C. to 130° C. prior to said calcining, for a period of time of from one hour to six hours.

16. The method of claim 1 , wherein the calcining is carried out at a temperature of from 300° C. to 700° C., after drying.

17. The method of claim 1 , wherein the calcining is carried out for a period of time of from one hour to four hours.

18. The method of claim 1 , wherein the calcining is carried out at a temperature of 800° C. or higher, and the calcined product comprises greater than 50% by weight the rutile polymorph.

19. The method of claim 1 , further comprising milling the calcined product in a fluid energy mill driven by air.

20. The method of claim 1 , wherein the calcined product has an average particle diameter of less than 40 nm.

Assignments (5)
SECURITY INTEREST Recorded Sep 26, 2025
From: TRONOX LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 072942/0255 →
RELEASE OF SECURITY INTEREST Recorded Apr 7, 2022
From: WILMINGTON TRUST, NATIONAL ASSOCIATION
To: TRONOX LLC
Reel/Frame 059629/0581 →
SECURITY INTEREST Recorded Mar 12, 2021
From: TRONOX LLC
To: HSBC BANK USA, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 055579/0619 →
SECURITY INTEREST Recorded May 1, 2020
From: TRONOX LLC
To: WILMINGTON TRUST, NATIONAL ASSOCIATION, AS COLLATERAL AGENT
Reel/Frame 052554/0529 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 25, 2019
From: THE NATIONAL TITANIUM DIOXIDE CO. LTD. (CRISTAL)
To: TRONOX LLC
Reel/Frame 049583/0638 →