Ozonation of contaminated liquids under high pressure

• US 20030183584A1
• Filed: 04/02/2002
• Published: 10/02/2003
• Est. Priority Date: 04/02/2002
• Status: Active Grant

• Current Assignee: Leidos, Inc. (Leidos Holdings, Inc.)
• Original Assignee: Science Applications International Corporation
• Inventors: Capitani, Frank Salvatore, Templeton, John Hale, Zimmers, Steven Raymond, Delp, Daniel Allen, Galatro, Thomas John
• Granted Patent: US 6,780,331 B2
• Time in Patent Office: Days
• US Class Current: 210/760
• CPC Class Codes: B09C 1/002 involving in-situ ground water treatment
• CPC Class Codes: C02F 1/722 Oxidation by peroxides
• CPC Class Codes: C02F 1/78 with ozone C02F1/4672 takes precedence
• CPC Class Codes: C02F 2103/06 Contaminated groundwater or leachate
• CPC Class Codes: C02F 2209/03 Pressure
• CPC Class Codes: C02F 2301/066 Overpressure, high pressure

Abstract

Contaminated liquids are treated by ozonation in a pressurized environment. Ozone is injected into a contaminated liquid to form a gas/liquid mixture. The mixture is injected into a mixing chamber for providing turbulent gas/liquid contact. The mixture is flowed from the mixing chamber into a pressurized reaction vessel. In an alternative embodiment, contaminated liquid is treated in situ using pressurized injection wells for injecting ozone-containing liquid.

Claims

1. A process of treating contaminated liquid by reaction with ozone in a pressurized reactor vessel, the method comprising:

injecting ozone into a contaminated liquid to form a gas/liquid mixture;

injecting said mixture into a mixing chamber for providing turbulent gas/liquid contact; and

flowing said mixture from said mixing chamber into said pressurized reactor vessel, wherein a pressure of at least about 45 psig is maintained in said reactor vessel.

2. A process of treating contaminated liquid by reaction with ozone in a pressurized reactor vessel, the method comprising:

injecting ozone into a contaminated liquid to form a gas/liquid mixture;

combining said gas/liquid mixture with recirculated headspace gas from said reactor vessel to form a reactive mixture having an air-to-liquid ratio of from about 0.25;

1 to about 10;

1;

injecting said reactive mixture into a mixing chamber for providing turbulent gas/liquid contact; and

flowing said reactive mixture from said mixing chamber into said pressurized reactor vessel, wherein a pressure of at least about 45 psig is maintained in said reactor vessel.

3. The process of claim 2 wherein a temperature of from about 35°

F. to about 70°

F. is maintained in said reactor vessel.

4. The process of claim 2 wherein said contaminated liquid contains a contaminant selected from the group consisting of MTBE, vinyl chloride, methylene chloride, ammonia, arsenic, benzene, ethylbenzene, tetrachloroethene, trichoroethene, toluene, xylene, and mixtures thereof.

5. The process of claim 2 wherein said pressure in said reactor vessel is at least about 50 psig.

6. The process of claim 5 wherein said pressure in said reactor vessel is at least about 80 psig.

7. The process of claim 2 further comprising combining a second oxidizer with said contaminated liquid.

8. The method of claim 7 wherein said second oxidizer comprises hydrogen peroxide.

9. The process of claim 2 wherein said air-to-liquid ratio is about 0.5:

1 to about 10;

1.

10. The process of claim 9 wherein said air-to-liquid ratio is about 1:

1 to about 10;

1.

11. A process of treating contaminated liquid in situ by reaction with ozone in a pressurized environment, the method comprising:

injecting influent liquid into a pressurized vessel;

injecting ozone into a recirculated stream from said vessel to form a gas/liquid mixture;

combining said gas/liquid mixture with recirculated headspace gas from said vessel to form a reactive mixture having an air-to-liquid ratio of from about 0.25;

1 to about 10;

1;

injecting said reactive mixture into a mixing chamber for providing turbulent gas/liquid contact;

flowing said reactive mixture from said mixing chamber into said vessel, wherein a pressure of at least about 45 psig is maintained in said vessel; and

injecting said reactive mixture into the ground.

12. The process of claim 11 wherein a temperature of from about 35°

F. to about 70°

F. is maintained in said vessel.

13. The process of claim 11 wherein said contaminated liquid contains a contaminant selected from the group consisting of MTBE, vinyl chloride, methylene chloride, ammonia, arsenic, benzene, ethylbenzene, tetrachloroethene, trichoroethene, toluene, xylene, and mixtures thereof.

14. The process of claim 11 wherein said pressure in said vessel is at least about 50 psig.

15. The process of claim 14 wherein said pressure in said vessel is at least about 80 psig.

16. The process of claim 11 wherein the reactive mixture is further pressurized to an injection pressure of at least about 80 psig prior to injection into the ground.

17. The process of claim 16 wherein said injection pressure is at least about 90 psig.

18. The process of claim 17 wherein said injection pressure is at least about 100 psig.

19. The process of claim 11 wherein the reactive mixture is injected into the ground to an injection depth of at least about 75 feet.

20. The process of claim 19 wherein said injection depth is at least about 100 feet.

21. The process of claim 20 wherein said injection depth is at least about 150 feet.

22. The process of claim 11 wherein said air-to-liquid ratio is about 0.5:

1 to about 10;

1.

23. The process of claim 22 wherein said air-to-liquid ratio is about 1:

1 to about 10;

1.

24. An apparatus for treating contaminated liquid by reaction with ozone in a pressurized reactor vessel, the apparatus comprising:

a conduit for feeding an influent liquid;

an ozone generator;

a first gas injector for injecting ozone into the influent liquid to form a gas/liquid mixture;

a second gas injector for injecting recirculated headspace gas from said reactor vessel into said gas/liquid mixture to form a reactive mixture;

a mixing chamber for providing turbulent mixing conditions for said reactive mixture; and

a generally enclosed reactor vessel for maintaining said reactive mixture in a pressurized environment.

25. The apparatus of claim 24 wherein said mixing chamber comprises a generally cylindrical member and an injection pipe having a plurality of nozzles for providing turbulent mixing conditions within said generally cylindrical member.

26. The apparatus of claim 24 wherein said mixing chamber is located within said reactor vessel.

27. The apparatus of claim 24 further comprising a pressurized injection well for injecting said reactive mixture into the ground.