IP Library Granted Patent US 11,305,231
Granted Patent B2
US 11,305,231 · App. 16/769,158 · Granted Apr 19, 2022

Pollutant treatment process and apparatus

Inventors: Damodara M. Poojary (Van Buren Township, MI); Jacques F. Nicole (Van Buren Township, MI); Matthew Keenan (Sussex, GB)
Assignee: Ricardo Inc.
B01D53/8628B01D53/8625B01D53/8668B01D53/9409B01J23/745B01J35/0006B01J37/0201B01J37/0236B01J37/088C01B3/40B01D53/92B01D2251/104B01D2255/20738B01D2255/30B01D2256/16B01D2257/404B01D2257/702B01D2258/012B01D2258/014B01D2258/0283C01B2203/0261C01B2203/1047C01B2203/1082C01B2203/1235C01B2203/1247
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Quick Facts
Patent No.
US 11,305,231
App. No.
16/769,158
Granted
Apr 19, 2022
Kind
B2
Abstract

A process for removing hydrocarbons from a feed stream containing hydrocarbons includes introducing ozone to the feed stream to produce an ozone doped stream containing ozone and hydrocarbons, and contacting the ozone doped stream with a supported metal catalyst at a temperature of from 100° C. to 300° C. to produce a treated stream, wherein the supported metal catalyst comprises iron supported on a support selected from aluminosilicates, silica-aluminas, silicates and aluminas. A process for removing NOx from a feed stream containing NOx, and an apparatus for removing hydrocarbons and/or NOx from a feed stream containing hydrocarbons and/or NOx are also provided.

Claims (26)

1. An apparatus for removing hydrocarbons and/or NO x from a feed stream containing hydrocarbons and/or NO x , the apparatus comprising:

a source of ozone arranged to introduce ozone to the feed stream to produce an ozone doped stream containing ozone and hydrocarbons and/or NO x ;

a supported metal catalyst comprising iron supported on a support selected from aluminosilicates, silica-aluminas, silicates and aluminas;

wherein the apparatus is arranged to contact the ozone doped stream with the supported metal catalyst at a temperature of from 100° C. to 300° C.

2. The apparatus of claim 1 , wherein the support of the supported metal catalyst comprises beta zeolite.

3. The apparatus of claim 1 , wherein the apparatus is arranged to receive an exhaust stream from a hydrocarbon combustion process or a waste gas stream from an industrial process as at least a portion of the feed stream.

4. The apparatus of claim 3 , further comprising means for carrying out hydrocarbon combustion and feeding an exhaust stream to the apparatus as at least a portion of the feed stream.

5. The apparatus of claim 4 , wherein the means for carrying out hydrocarbon combustion comprises a natural gas engine.

6. The apparatus of claim 1 , wherein the apparatus is configured so that the ozone doped stream is contacted with the supported metal catalyst at a temperature of from 130° C. to 280° C.

7. The apparatus of claim 1 , wherein the apparatus is configured to provide a flow of the ozone doped stream over the supported metal catalyst continuously for greater than 1 minute.

8. The apparatus of claim 1 , wherein the apparatus is configured to contact the ozone doped stream with the supported metal catalyst at a pressure of 10 bar absolute or less.

9. The apparatus of claim 1 , wherein the source of ozone comprises an ozone generator configured to generate ozone in situ.

10. The apparatus of claim 9 , wherein the ozone generator comprises a corona discharge ozone generator, a cold plasma ozone generator or a UV ozone generator.

11. An industrial processing plant comprising the apparatus of claim 1 for reducing emissions of hydrocarbons and/or NO x .

12. A vehicle comprising the apparatus of claim 1 for reducing emissions of hydrocarbons and/or NO x .

13. A process for removing methane from a feed stream containing methane using the apparatus of claim 1 , the process comprising:

using a source of ozone to generate ozone and introducing the ozone to a feed stream containing methane to produce an ozone doped stream containing ozone and methane; and

contacting the ozone doped stream with a supported metal catalyst at a temperature of from 100° C. to 300° C. produce a treated stream;

wherein the supported metal catalyst comprises iron supported on a support selected from aluminosilicates, silica-aluminas, silicates and aluminas.

14. The process of claim 13 , wherein the ozone doped stream is contacted with the supported metal catalyst at a temperature of from 130° C. to 280° C.

15. The process of claim 13 , wherein the support of the supported metal catalyst comprises a zeolite support.

16. The process of claim 13 , wherein the contacting step comprises providing a flow of the ozone doped stream over the supported metal catalyst continuously for greater than 1 minute.

17. The process of claim 13 , wherein the contacting step is conducted at a pressure of 10 bar absolute or less.

18. The process of claim 13 , wherein the feed stream comprises an exhaust stream from a natural gas engine.

19. The process of claim 13 , wherein the ozone introduced to the feed stream is generated by an ozone generator in situ.

20. The process of claim 13 , wherein water is present in the feed stream or the ozone doped stream in an amount of up to 15% v/v.

Assignments (3)
CHANGE OF NAME Recorded Nov 19, 2024
From: RICARDO, INC.
To: RICARDO LLC
Reel/Frame 069389/0477 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 15, 2020
From: KEENAN, MATTHEW
To: RICARDO UK LIMITED
Reel/Frame 053774/0572 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Sep 15, 2020
From: POOJARY, DAMODARA M.; NICOLE, JACQUES F.
To: RICARDO INC.
Reel/Frame 053774/0740 →
Continuity (2)
Continuation 15830701 · Dec 4, 2017
Related Publication 20210113962A1 · Apr 22, 2021