IP Library › Granted Patent US 8,740,195
Granted Patent B2
US 8,740,195 · App. 13/678,444 · Granted Jun 3, 2014

Systems and methods for diffusing gas into a liquid

Inventors: Jakob H. Schneider (Calgary, CA); Joseph Mark Schneider (Fonthill, CA)
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Quick Facts
Patent No.
US 8,740,195
App. No.
13/678,444
Granted
Jun 3, 2014
Kind
B2
Abstract

Systems and methods for diffusing gas into a liquid are disclosed. In some cases, the methods include tangentially introducing a liquid into a cylindrical chamber having a cylindrical inner wall such that the liquid develops a spiral flow. In some cases, gas bubbles are orthogonally introduced into the liquid as the liquid flows through the chamber. In some cases, a flow of the liquid and the gas bubbles is controlled such that a ratio of a liquid flow rate to a gas bubble flow rate does not exceed values which convert non-bacteria enriched, clear water into froth. In such cases, a mixture of the liquid and the gas bubbles to exit the chamber near an output end. While the liquid can include clear water, in some instances, the liquid also includes bacteria (e.g., surfactant-producing or non-surfactant-producing bacteria) and/or bacterial nutrients that allow for improved bioremediation.

Claims (39)

1. A process for diffusing gas bubbles in a liquid, the process comprising:

i) introducing a stream of the liquid into a cylindrical chamber having a cylindrical inner wall, and enclosed at a first end, the stream being introduced tangentially at an input zone near the first end of the chamber in a manner to develop a spiral flow of the stream along the cylindrical inner wall toward an opposite, output end of the chamber, wherein the stream comprises at least one of clear water and a fluid enriched with bacteria,

ii) introducing gas into the stream during at least a portion of its travel in the chamber, the gas being introduced to the stream orthogonally through means located at the chamber inner wall for developing gas bubbles which move into the stream,

iii) controlling a flow of the liquid and the gas bubbles so that a ratio of liquid flow rate to gas bubble flow rate does not exceed values which convert non-bacteria enriched, clear water into froth,

iv) the chamber being of a length sufficient to provide a residence time in the chamber which permits a diffusion of the gas in the liquid, and

v) allowing a mixture of the liquid and the gas bubbles to exit the chamber near the output end.

2. The process of claim 1 , wherein the stream comprises the fluid enriched with bacteria, and wherein the bacteria comprises a surfactant-producing bacteria that is capable of producing a surfactant that alters a surface tension of the gas bubbles such that the mixture of liquid and gas bubbles comprises a froth as it exits the chamber.

3. The process of claim 1 , further comprising adding bacterial nutrients to the stream.

4. The process of claim 2 , wherein the gas comprises oxygen.

5. The process of claim 1 , wherein the stream comprises the fluid enhanced with bacteria, and wherein the bacteria comprises a non-surfactant-producing bacteria, such that the mixture of the liquid and the gas bubbles exits the chamber substantially free of froth.

6. The process of claim 1 , wherein the chamber is operable in any and all orientations.

7. A process for diffusing gas bubbles in a liquid, the process comprising:

i) introducing a stream of the liquid into a cylindrical chamber having a cylindrical inner wall, and enclosed at a first end, the stream being introduced tangentially at an input zone near the first end of the chamber in a manner to develop a spiral flow of the stream along the cylindrical inner wall toward an opposite, output end of the chamber, wherein the stream comprises clear water,

ii) introducing gas into the stream during at least a portion of its travel in the chamber, the gas being introduced to the stream orthogonally through means located at the chamber inner wall for developing gas bubbles which move into the stream,

iii) controlling a flow of the liquid and the gas bubbles so that a ratio of liquid flow rate to gas bubble flow rate does not exceed values which convert non-bacteria enriched, clear water into froth,

iv) the chamber being of a length sufficient to provide a residence time in the chamber which permits a diffusion of the gas in the liquid, and

v) allowing a mixture of the liquid and the gas bubbles to exit the chamber near the output end.

8. The process of claim 7 , further comprising adding surfactant-producing bacteria to the stream, wherein the surfactant-producing bacteria produces a surfactant that alters a surface tension of the gas bubbles such that the mixture of liquid and gas bubbles comprises a froth as it exits the chamber.

9. The process of claim 7 , further comprising adding a non-surfactant-producing bacteria to the stream, such that the mixture of the liquid and the gas bubbles exits the chamber substantially free of froth.

10. The process of claim 7 , further comprising applying the froth to an application site.

11. The process of claim 10 , wherein the application site comprises an in situ site.

12. The process of claim 10 , wherein the application site comprises a surface of a body of water.

13. The process of claim 12 , wherein the body of water comprises a volatile organic compound, and wherein the froth traps a portion of the volatile organic compound in an aerobic environment, re-entrains the portion of the volatile organic compound into the body of water, and reduces odors being released into the atmosphere from the portion of the volatile organic compound.

14. The process of claim 7 , wherein the introduction of gas into the stream during at least a portion of its travel in the chamber produces a gas-rich froth that enhances an environment for bacteria.

15. The process of claim 14 , wherein the gas comprises oxygen and the gas-rich froth comprises an oxygen-rich froth.

16. The process of claim 7 , further comprising adding bacterial nutrients to the stream.

17. The process of claim 7 , wherein the chamber is operable in any and all orientations.

18. A process for diffusing gas bubbles in a liquid, the process comprising:

i) introducing a stream of the liquid into a cylindrical chamber having a cylindrical inner wall, and enclosed at a first end, the stream being introduced tangentially at an input zone near the first end of the chamber in a manner to develop a spiral flow of the stream along the cylindrical inner wall toward an opposite, output end of the chamber,

ii) introducing gas into the stream during at least a portion of its travel in the chamber, the gas being introduced to the stream orthogonally through means located at the chamber inner wall for developing gas bubbles which move into the stream,

iii) adding bacteria to the stream, wherein the bacteria is selected from a surfactant-producing bacteria and a non-surfactant-producing bacteria,

iv) controlling a flow of the liquid and the gas bubbles so that a ratio of liquid flow rate to gas bubble flow rate does not exceed values which convert non-bacteria enriched, clear water into froth,

v) the chamber being of a length sufficient to provide a residence time in the chamber which permits a diffusion of the gas in the liquid, and

vi) allowing a mixture of the liquid and the gas bubbles to exit the chamber near the output end.

19. The process of claim 18 , wherein the bacteria comprises the surfactant-producing bacteria, and the surfactant-producing bacteria produce a surfactant that alters a surface tension of the gas bubbles such that the mixture of liquid and gas bubbles comprises a froth as it exits the chamber.

20. The process of claim 18 , wherein the bacteria comprises the non-surfactant-producing bacteria, such that the mixture of the liquid and the gas bubbles exits the chamber substantially free of froth.

21. The process of claim 18 , further comprising adding bacterial nutrients to the stream to enhance a multiplication of the bacteria.

22. The process of claim 18 , wherein the stream comprises clear water.

23. The process of claim 18 , wherein the chamber is operable in any and all orientations.

Assignments (1)
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jan 6, 2015
From: SCHNEIDER, JAKOB H.; SCHNEIDER, JOSEPH MARK
To: HYDRO PROCESSING & MINING LTD.
Reel/Frame 034645/0512 →
Priority Claims (2)
CA 2534704 · Jan 31, 2007 · national
WO PCT/CA2007/000160 · Jan 31, 2007 · international
Continuity (3)
Continuation In Part 13620069 · Sep 14, 2012
Division 12162603 · Jul 29, 2008
Related Publication 20130163372A1 · Jun 27, 2013