IP Library Granted Patent US 7,114,533
Granted Patent B2
US 7,114,533 · App. 10/949,691 · Granted Oct 3, 2006

Densification of aerated powders using positive pressure

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Quick Facts
Patent No.
US 7,114,533
App. No.
10/949,691
Granted
Oct 3, 2006
Kind
B2
Abstract

A process for increasing the bulk density of an aerated powder is provided. The powder is placed in a container. The container is then closed and the gas pressure within the container is increased to a level above atmospheric pressure and at a rate sufficient to cause the powder to compact before a substantial portion of said pressurization gas diffuses into said powder. In one embodiment, the process is utilized to increase the bulk density of an aerated, free-flowing titanium dioxide pigment. Apparatus for carrying out the process is also provided.

Claims (32)

1. An apparatus for increasing the bulk density of a powder, comprising:

a container for containing said powder under pressure, said container having an internal area containing said powder, a first end and a second end opposing said first end; and

pressurization means associated with the internal area of said container containing said powder, said pressurization means injects a pressurized gas into the internal area to rapidly increase internal gas pressure in the internal area of said container containing said powder to a level above atmospheric pressure and thereby compacting said powder, other than by decreasing the volume of the internal area of the container containing said powder, at a rate sufficient to cause said powder to compact before a substantial portion of the gas in the internal area of said container containing said powder diffuses into said powder, wherein said powder is compacted by the rapid increase of internal gas pressure without the use of any mechanical device applied to said powder;

said container having a first end including an inlet for allowing said powder to be added to said container and a second end opposing said first end, said second end including an outlet for depressurizing said container and for removing said powder from said container, said container comprising a first valve for opening and closing said inlet and a second valve for opening and closing said outlet, whereby depressurization of said container and gravity expels said powder from said container through said outlet of said container.

2. The apparatus of claim 1 wherein said source of gas provides a gas selected from the group consisting of an inert gas, air, nitrogen, oxygen, carbon dioxide and chlorine gas.

3. The apparatus of claim 1 wherein said pressurization means causes said powder to compact against said outlet when said outlet is closed.

4. A process for increasing the bulk density of an aerated powder, comprising:

placing said powder into a container, said container having an internal area containing said powder, a first end and a second end opposing said first end;

compacting said powder against said second end solely by injecting a pressurized gas into said internal area to rapidly increase internal gas pressure in the internal area of said container containing said powder to a level above atmospheric pressure at a rate sufficient to cause said powder to compact against said second end of said container, wherein said powder is compacted against said second end by the rapid increase of internal gas pressure without the use of any mechanical device applied to said powder;

depressurizing and emptying said container by opening said second end of said container whereby depressurization of said container and gravity expels said powder from said container through said second end of said container.

5. The process of claim 4 wherein said gas injected into said container is selected from the group consisting of an inert gas, air, nitrogen, oxygen, carbon dioxide and chlorine.

6. The process of claim 4 wherein said powder is an inorganic metal oxide.

7. The process of claim 4 wherein said powder is a titanium dioxide pigment.

8. The process of claim 7 wherein the bulk density of said titanium dioxide pigment is increased to a level greater than about 35 lbs/ft 3 .

9. The process of claim 7 wherein the bulk density of said titanium dioxide pigment is increased to a level in the range of from about 40 lbs/ft 3 to about 50 lbs/ft 3 .

10. The process of claim 4 wherein said powder comprises a battery-active material.

11. The process of claim 10 wherein said battery-active material is selected from the group of metal oxides and metal phosphates wherein said metal is vanadium, manganese, nickel, cobalt, iron or a combination thereof.

12. The process of claim 10 wherein said battery-active material is selected from the group of lithium metal oxides and lithium metal phosphates wherein said metal is vanadium, manganese, nickel, cobalt, iron or a combination thereof.

13. The process of claim 10 wherein the bulk density of said battery-active material is increased by at least about 10 percent.

14. The process of claim 10 wherein the bulk density of said battery-active material is increased by at least about 15 percent.

15. A process for increasing the bulk density of an aerated powder, comprising:

placing said powder into a container, said container having an internal area containing said powder, a first end and a second end opposing said first end, and a valve associated with said second end for emptying said container;

compacting said powder against said second end solely by injecting a pressurized gas into the internal area to rapidly increase internal gas pressure in the internal area of said container to a level above atmospheric pressure, wherein said pressurization does not decrease the overall volume of the internal area of said container containing said powder, said pressurization occurs at a rate sufficient to cause said powder to compact against said second end of said container, wherein said powder is compacted against said second end by the rapid increase of internal gas pressure without the use of any mechanical device applied to said powder;

depressurizing and emptying said container by opening said valve associated with said second end of said container whereby depressurization of said container and gravity expels said powder from said container through said second end of said container.

16. The process of claim 15 wherein said gas injected into said container is selected from the group consisting of an inert gas, air, nitrogen, oxygen, carbon dioxide and chlorine.

17. The process of claim 15 wherein said powder is an inorganic metal oxide.

18. The process of claim 15 wherein said powder is a titanium dioxide pigment.

19. The process of claim 18 wherein the bulk density of said titanium dioxide pigment is increased to a level greater than about 35 lbs/ft 3 .

20. The process of claim 15 wherein said powder comprises a battery-active material.

21. The process of claim 20 wherein said battery-active material is selected from the group of metal oxides and metal phosphates wherein said metal is vanadium, manganese, nickel, cobalt, iron or a combination thereof.

22. The process of claim 20 wherein said battery-active material is selected from the group of lithium metal oxides and lithium metal phosphates wherein said metal is vanadium, manganese, nickel, cobalt, iron or a combination thereof.

23. The process of claim 20 wherein the bulk density of said battery-active material is increased by at least about 10 percent.

Assignments (15)
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 →
RELEASE OF SECURITY INTEREST Recorded Mar 12, 2021
From: WELLS FARGO BANK, NATIONAL ASSOCIATION
To: TRONOX LLC
Reel/Frame 055583/0001 →
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 →
SECURITY INTEREST Recorded Sep 25, 2017
From: TRONOX LLC
To: WELLS FARGO BANK, NATIONAL ASSOCIATION
Reel/Frame 043993/0340 →
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 →
BANKRUPTCY COURT NOTICE CONFIRMING RELEASE OF LIENS EFFECTIVE 2/14/2011 Recorded Mar 24, 2011
From: LEHMAN COMMERCIAL PAPER, INC.
To: TRONOX LLC
Reel/Frame 026010/0684 →
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 →
SECURITY AGREEMENT Recorded Aug 21, 2008
From: TRONOX LLC F/K/A KERR-MCGEE CHEMICAL LLC
To: LEHMAN COMMERCIAL PAPER INC.
Reel/Frame 021411/0792 →
CHANGE OF NAME Recorded Aug 15, 2008
From: KERR-MCGEE CHEMICAL LLC
To: TRONOX LLC
Reel/Frame 021411/0498 →