IP Library Granted Patent US 6,916,359
Granted Patent B2
US 6,916,359 · App. 10/419,395 · Granted Jul 12, 2005

Ozone production processes

Assignee: The BOC Group, Inc.
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Quick Facts
Patent No.
US 6,916,359
App. No.
10/419,395
Granted
Jul 12, 2005
Kind
B2
Abstract

Methods of providing ozone at a selected pressure above atmospheric pressure include supplying a purge gas supply ( 22 ) pressurized above the selected pressure to at least one ozone adsorption apparatus ( 12 ); desorbing ozone from the ozone adsorption apparatus ( 12 ) with the pressurized purge gas supply ( 22 ); and delivering a mixture of ozone and the purge gas supply ( 24 ) at the selected pressure without further compression.

Claims (50)

1. A method of providing ozone at a selected pressure above atmospheric pressure comprising:

supplying a purge gas supply pressurized above the selected pressure to at least one ozone adsorption apparatus;

desorbing ozone from said ozone adsorption apparatus with said pressurized purge gas supply; and

delivering a mixture of said ozone and said purge gas supply at the selected pressure without further compression.

2. The method according to claim 1 wherein the pressurized purge gas supply supplied to at least one ozone adsorption apparatus is selected from the group consisting of a compressed dry air supply and a nitrogen supply.

3. The method according to claim 1 further comprising:

compressing a supply of air to provide a compressed air supply;

supplying said compressed air supply to an oxygen generator; and,

generating an oxygen supply with said oxygen generator.

4. The method according to claim 3 wherein said oxygen generator generating said oxygen supply comprises at least one dryer bed and at least one nitrogen adsorbing bed arranged in series.

5. The method according to claim 4 wherein a compressed dry air supply exits said dryer bed, and a first part of said compressed dry air supply is directed to said nitrogen adsorbing bed and a second part of said compressed dry air supply becomes said pressurized purge gas supply.

6. The method according to claim 3 wherein said oxygen generator generating said oxygen supply comprises at least one air prepurification unit and a cryogenic unit arranged in series.

7. The method according to claim 6 wherein said air prepurification unit removes contaminants from said compressed air supply to form a purified compressed air supply exiting said air prepurification unit, and said purified compressed air supply is directed to said cryogenic unit.

8. The method according to claim 7 wherein said cryogenic unit separates said purified compressed air supply into said oxygen supply and a nitrogen supply, and said nitrogen supply becomes said pressurized purge gas supply.

9. The method according to claim 3 wherein said oxygen generator generating said oxygen supply comprises at least one dryer bed, at least one air prepurification unit, and a cryogenic unit arranged in series.

10. The method according to claim 9 wherein a compressed dry air supply exits said dryer bed, and a first part of said compressed dry air supply is directed to said air prepurification unit and a second part of said compressed dry air supply becomes said pressurized purge gas supply.

11. The method according to claim 10 wherein a dry purified compressed air supply exits said air prepurification unit, and said dry purified air supply is directed to said cryogenic unit.

12. The method according to claim 11 wherein said cryogenic unit at least partially separates said dry purified compressed air supply into said oxygen supply and a nitrogen supply.

13. The method according to claim 3 further comprising:

directing said oxygen supply to an ozone generator; and

generating an ozone-rich oxygen supply using said ozone generator.

14. The method according to claim 13 further comprising:

directing said ozone-rich oxygen supply to said at least one ozone adsorption apparatus;

adsorbing ozone from said ozone-rich oxygen supply in said at least one ozone adsorption apparatus to form an ozone-depleted oxygen supply; and

recycling the ozone-depleted oxygen supply to said ozone generator.

15. The method according to claim 14 further comprising:

mixing said ozone-depleted oxygen supply with a vaporized liquid oxygen supply having an elevated pressure to form a compressed mixed oxygen supply; and,

directing the compressed mixed oxygen supply to said ozone generator.

16. The method according to claim 1 further comprising:

supplying said at least one ozone adsorption apparatus with a high purity oxygen supply;

purging said pressurized purge gas supply from said at least one ozone adsorption apparatus using said high purity oxygen supply; and

pressurizing said at least one ozone adsorption apparatus with said high purity oxygen supply.

17. The method according to claim 1 further comprising:

warming said pressurized purge gas supply before entering said at least one ozone adsorption apparatus.

18. The method according to claim 1 including at least one of

compressing ambient air to a desorption pressure above the selected pressure to provide the pressurized purge gas supply; and

introducing said pressurized purge gas supply to desorb ozone from said ozone adsorption apparatus without first drying said pressurized purge gas supply.

19. The method according to claim 1 including directing an ozone-rich oxygen supply to at least a second ozone adsorption apparatus while desorbing ozone from said at least one ozone adsorption apparatus with said pressurized purge gas supply; to provide a constant supply of gas containing ozone.

20. A method of providing ozone at a selected pressure above atmospheric pressure comprising:

providing a supply of compressed dry air at a pressure above the selected pressure;

diverting a first portion of said compressed dry air supply to an oxygen generator;

generating an oxygen supply with said oxygen generator;

directing said oxygen supply to an ozone generator;

generating an ozone-rich oxygen supply with said ozone generator;

passing said ozone-rich oxygen supply through at least one pressure swing adsorption tower;

adsorbing ozone from said ozone-rich oxygen supply in said pressure swing adsorption tower, to provide an ozone-depleted oxygen supply;

recycling the ozone-depleted oxygen supply to said ozone generator;

diverting a second portion of said compressed dry air supply to said pressure swing adsorption tower;

desorbing said ozone from said pressure swing adsorption tower using said second portion of said compressed dry air supply; and

delivering a mixture of said ozone from said pressure swing adsorption tower and said second portion of said compressed air supply at the selected pressure without further compression.

Assignments (6)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 7, 2019
From: MESSER LLC
To: MESSER INDUSTRIES USA, INC.
Reel/Frame 049983/0990 →
MERGER Recorded Jun 28, 2019
From: LINDE, INC.
To: LINDE LLC
Reel/Frame 049622/0560 →
CHANGE OF NAME Recorded Jun 28, 2019
From: THE BOC GROUP, INC.
To: LINDE, INC.
Reel/Frame 049635/0975 →
CHANGE OF NAME Recorded Jun 28, 2019
From: LINDE LLC
To: MESSER LLC
Reel/Frame 049636/0001 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Aug 25, 2003
From: JAIN, RAVI
To: BOC GROUP, INC., THE
Reel/Frame 013905/0676 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded May 29, 2003
From: JAIN, RAVI
To: BOC GROUP, INC., THE
Reel/Frame 014111/0680 →
Continuity (2)
Provisional Application 6037556000 · Apr 25, 2002
Related Publication 20040028576A1 · Feb 12, 2004