IP Library Patent Application 11187470
Patent Application
App. No. 11/187,470

Scour media for titanium dioxide production

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Quick Facts
Patent No.
US None
App. No.
11/187,470
Abstract

Anatase titanium dioxide pigment calcined to a crush strength and density meeting the requirements for an acceptable scour medium is effectively utilized as a scour medium in the chloride process for producing rutile titanium dioxide. The calcining process converts a portion of the anatase pigment to rutile. This calcined anatase can, consequently, be utilized as a scour medium in the chloride process for producing rutile titanium dioxide. The calcined anatase is not a contaminant to the process for producing rutile titanium dioxide. Thus, relatively inexpensive anatase can be converted into a rutile scour medium that can be processed into pigment.

Claims (35)

1 - 7 . (canceled)

8 . A method for producing rutile titanium dioxide, comprising the steps of:

calcining anatase titanium dioxide to a crush strength of less than about 30; and

introducing the calcined anatase into equipment for the production of rutile titanium dioxide.

9 . A method according to claim 8 , wherein the equipment is for the production of rutile titanium dioxide via the chloride process.

10 . A method according to claim 8 , wherein the anatase is calcined to a crush strength of greater than about 15.

11 . A method according to claim 8 , wherein the calcining step takes place at a temperature greater than about 1025° C.

12 . A method according to claim 8 , wherein the calcining step takes place at a temperature from about 1025° C. to about 1075° C.

13 . A method according to claim 8 , wherein the anatase is calcined to a density of from about 1.55 g/cm 3 to about 1.71 g/cm 3 .

14 . A method according to claim 8 , wherein the calcined anatase is introduced into an oxidation reactor.

15 . A method according to claim 8 , wherein the calcined anatase is introduced into a cooling conduit.

16 . A method for producing rutile titanium dioxide, comprising the steps of:

obtaining anatase titanium dioxide from an anatase production process;

calcining the anatase titanium dioxide to a crush strength of less than about 30; and

introducing the calcined anatase into equipment for the production of rutile titanium dioxide.

17 . A method according to claim 16 , wherein the anatase production process is a sulfate process for the production of anatase titanium dioxide.

18 . A method according to claim 16 , wherein the obtained anatase is obtained from calciner discharge from an anatase production process.

19 . A method according to claim 16 , wherein the anatase is calcined to a crush strength greater than about 15.

20 . A method for producing rutile titanium dioxide, comprising the steps of:

obtaining anatase titanium dioxide from a sulfate process for the production of anatase titanium dioxide;

calcining the anatase titanium dioxide to a crush strength of less than about 30 and greater than about 15; and

introducing the calcined anatase into equipment for the production of rutile titanium dioxide via the chloride process.

21 . A method according to claim 20 , wherein the calcining step takes place at a temperature greater than about 1025° C.

22 . A method according to claim 20 , wherein the calcining step takes place at a temperature from about 1025° C. to about 1075° C.

23 . A method according to claim 20 , wherein the anatase is calcined to a density of from about 1.55 g/cm 3 to about 1.71 g/cm 3 .

24 . A method according to claim 20 , wherein the calcined anatase is introduced into an oxidation reactor.

25 . A method according to claim 20 , wherein the calcined anatase is introduced into a cooling conduit.

26 . A method for producing rutile titanium dioxide, comprising the steps of:

obtaining anatase titanium dioxide from a sulfate process for the production of anatase titanium dioxide;

calcining the anatase titanium dioxide to a crush strength of less than about 30 and greater than about 15;

introducing the calcined anatase into equipment for the production of rutile titanium dioxide via the chloride process; and

producing titanium dioxide containing no more than about 2 percent by weight of anatase.

27 . A method according to claim 26 , wherein the producing step produces titanium dioxide containing no more than about 1 percent by weight of anatase.

28 . A method according to claim 26 , wherein the introduced calcined anatase comprises no more than about 5 percent of the produced titanium dioxide.

29 . A method according to claim 26 , wherein the introduced calcined anatase comprises no less than about 2.5 percent of the produced titanium dioxide.

Assignments (10)
ASSIGNMENT OF SECURITY INTEREST IN PATENT COLLATERAL RECORDED AT REEL/FRAME 044100/0339 Recorded Mar 12, 2021
From: BANK OF AMERICA, N.A.
To: HSBC BANK USA, NATIONAL ASSOCIATION, AS THE SUCCESSOR ADMINISTRATIVE AGENT AND COLLATERAL AGENT
Reel/Frame 055578/0880 →
PATENT SECURITY AGREEMENT Recorded Oct 2, 2017
From: TRONOX LLC
To: BANK OF AMERICA, N.A., AS COLLATERAL AGENT
Reel/Frame 044100/0339 →
RELEASE OF SECURITY INTEREST IN INTELLECTUAL PROPERTY COLLATERAL AT REEL/FRAME NOS. 027682/0086 AND 030047/0422 Recorded Sep 26, 2017
From: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
To: TRONOX LLC
Reel/Frame 044018/0893 →
RELEASE OF SECURITY INTEREST IN PATENTS Recorded Sep 25, 2017
From: UBS AG, STAMFORD BRANCH, AS COLLATERAL AGENT
To: TRONOX LLC; TRONOX WORLDWIDE LLC
Reel/Frame 043993/0306 →
PATENT SECURITY AGREEMENT Recorded Jul 18, 2012
From: TRONOX LLC; TRONOX WORLDWIDE LLC
To: UBS AG, STAMFORD BRANCH
Reel/Frame 028582/0669 →
RELEASE OF SECURITY INTEREST IN PATENTS Recorded Jul 12, 2012
From: WELLS FARGO CAPITAL FINANCE, LLC
To: TRONOX LLC; TRONOX WORLDWIDE LLC
Reel/Frame 028535/0362 →
RELEASE OF SECURITY INTEREST Recorded Feb 9, 2012
From: GOLDMAN SACHS LENDING PARTNERS LLC
To: TRONOX LLC
Reel/Frame 027682/0064 →
SECURITY AGREEMENT Recorded Feb 9, 2012
From: TRONOX LLC
To: GOLDMAN SACHS BANK USA, AS COLLATERAL AGENT
Reel/Frame 027682/0086 →
SECURITY AGREEMENT Recorded Feb 22, 2011
From: TRONOX LLC; TRONOX PIGMENTS (SAVANNAH) INC.
To: WELLS FARGO CAPITAL FINANCE, LLC, AS AGENT
Reel/Frame 025822/0026 →
SECURITY AGREEMENT Recorded Feb 15, 2011
From: TRONOX LLC
To: GOLDMAN SACHS LENDING PARTNERS LLC, AS COLLATERAL AGENT
Reel/Frame 025795/0130 →