IP Library Granted Patent US 9,327,251
Granted Patent B2
US 9,327,251 · App. 14/166,567 · Granted May 3, 2016

System and method for improved gas dissolution

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Quick Facts
Patent No.
US 9,327,251
App. No.
14/166,567
Granted
May 3, 2016
Kind
B2
Abstract

The invention provides a microbubble generation system with increased efficiency and flexibility compared to known systems. Further, the invention provides a method of microbubble generation. In particular, invention relates to increasing the efficiency of a fermentation reaction by reducing bubble size and increasing gas absorption into a liquid fermentation broth.

Claims (20)

1. A method of generating microbubbles comprising:

(a) sparging gas into a column containing a liquid via a gas sparger to form gas bubbles wherein the gas bubbles migrate upward to the top of the liquid and form a foam layer; and

(b) introducing additional liquid to the column via an inlet positioned above a perforated plate, said perforated plate positioned above the gas sparger, wherein the foam layer is maintained below the perforated plate, the additional liquid passing downward through the perforated plate to form liquid jets such that the liquid jets contact the bubbles in the foam layer and produce microbubbles entrained in the liquid.

2. The method of claim 1 , wherein the perforated plate of step (b) comprises perforations with a diameter from about 0.1 to about 0.5 mm.

3. The method of claim 1 , wherein the liquid contained in the column or the additional liquid introduced to the column contains at least one surface active species selected from the group consisting of a protein, a peptide, an ionic surfactant, non-ionic surfactant, and a bio-surfactant.

4. The method of claim 1 , wherein the microbubbles produced have a diameter from about 10 to about 200 μm in diameter.

5. The method of claim 1 , further comprising passing at least a portion of the microbubble entrained liquid to a foam/liquid separator operated at conditions to produce a separated liquid stream and a separated foam stream.

6. The method of claim 5 , further comprising passing at least a portion of the separated liquid stream back to the perforated plate.

7. The method of claim 5 , further comprising passing at least a portion of the separated foam stream to a de-foaming tank.

8. The method of claim 1 , further comprising passing at least a portion of the microbubble entrained liquid to a gas/liquid separator to produce a separated gas stream and a separated liquid stream.

9. The method of claim 1 , further comprising releasing gas pressure from the column via a gas relief valve.

10. The method of claim 1 , further comprising providing at least a portion of the microbubble entrained liquid to a culture of at least one microorganism in a fermentation broth to form a second fermentation broth containing the microbubble entrained liquid and anaerobically fermenting the gas in the microbubbles to produce at least one product.

11. The method of claim 10 , wherein the microbubbles comprise CO.

12. The method of claim 10 , wherein the at least one product is selected from the group consisting of ethanol, butanol, 2,3-butanediol, acetone, isopropanol, acetic acid, lactic acid, and biomass.

13. The method of claim 10 , wherein the culture is located inside the column.

14. The method of claim 10 , wherein the culture is located in a bioreactor vessel.

15. The method of claim 14 , further comprising passing at least a portion of the second fermentation broth from the bioreactor vessel to a primary gas/liquid separator to form a separated gas stream and a separated third fermentation broth stream.

16. The method of claim 15 , further comprising passing at least a portion of the separated gas stream back to the column via the gas sparger.

17. The method of claim 15 , further comprising passing at least a portion of the separated third fermentation broth stream back to the column via the perforated plate.

18. The method of claim 17 , further comprising separating at least one product from the separated third fermentation broth stream prior to passing the third fermentation broth to the column via the perforated plate.

Assignments (6)
CORRECTIVE ASSIGNMENT TO CORRECT THE THE PATENT NUMBE 9,5348,20 PREVIOUSLY RECORDED AT REEL: 059911 FRAME: 0400. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 4, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ INC.
Reel/Frame 061084/0646 →
CORRECTIVE ASSIGNMENT TO CORRECT THE U.S. PATENT NUMBER 8,979,228 PREVIOUSLY RECORDED AT REEL: 059911 FRAME: 0400. ASSIGNOR(S) HEREBY CONFIRMS THE ASSIGNMENT. Recorded Aug 3, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ, INC.
Reel/Frame 061058/0076 →
RELEASE OF SECURITY INTEREST Recorded May 9, 2022
From: VENTURE LENDING & LEASING VII, INC.; VENTURE LENDING & LEASING VIII, INC.
To: LANZATECH NEW ZEALAND LIMITED; LANZATECH, INC.; LANZATECH FREEDOM PINES BIOREFINERY LLC; LANZATECH HONG KONG LIMITED; LANZATECH PRIVATE LIMITED; LANZATECH UK LIMITED
Reel/Frame 059910/0789 →
CHANGE OF NAME Recorded May 9, 2022
From: LANZATECH NEW ZEALAND LIMITED
To: LANZATECH NZ, INC.
Reel/Frame 059911/0400 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Jun 4, 2014
From: LI, XUELIANG
To: LANZATECH NEW ZEALAND LIMITED
Reel/Frame 033023/0168 →
ASSIGNMENT OF ASSIGNOR'S INTEREST Recorded Feb 3, 2014
From: LI, XUELIANG
To: LANZATECH NEW ZEALAND LIMITED
Reel/Frame 032120/0976 →