Photobioreactor systems positioned on bodies of water

• US 8,859,262 B2
• Filed: 07/18/2011
• Issued: 10/14/2014
• Est. Priority Date: 04/27/2007
• Status: Expired due to Fees

• Current Assignee: Algae Systems, LLC
• Original Assignee: Algae Systems, LLC
• Inventors: Berzin, Isaac, de Luis, Javier, Fair, David, Parrish, Joe, Polito, Benjamin F., Walker, Miles, Fowler, Ben, Lockwood, Kevin, Richtman, Keith, Chen, Fan, Olaizola, Miguel
• Primary Examiner(s): Beisner, William H
• Application Number:
  US13/185,403
• Publication Number:
  US 20110287544A1
• Time in Patent Office: 1,184 Days
• Field of Search: 435/292.1, 435/257.1, 47/14
• US Class Current: 435/257.1
• CPC Class Codes: C12M 21/02 Photobioreactors culturing algae A01G33/00, A01H4/001, C12N1/12
• CPC Class Codes: C12M 23/06 Tubular C12M23/08, C12M23/16 take precedence
• CPC Class Codes: C12M 23/26 flexible flexible containers for laboratory use B01L3/505
• CPC Class Codes: C12M 23/34 Internal compartments or partitions
• CPC Class Codes: C12M 23/56 Floating elements
• CPC Class Codes: C12M 27/06 with horizontal or inclined stirrer shaft or axis
• CPC Class Codes: C12M 29/06 Nozzles; Sprayers; Spargers; Diffusers per se B01F23/231, B01J19/26
• CPC Class Codes: C12M 41/18 Heat exchange systems, e.g. heat jackets or outer envelopes

Abstract

Certain embodiments and aspects of the present invention relate to a photobioreactor including photobioreactor units through which a liquid medium stream and a gas stream flow. The photobioreactor units are floated on a body of water such as a pond or a lake. The liquid medium comprises at least one species of phototrophic organism therein. Certain methods of using the photobioreactor system as part of fuel generation system and/or a gas-treatment process or system at least partially remove certain undesirable pollutants from a gas stream. In certain embodiments, the photobioreactor units are formed of flexible, deformable material and are configured to provide a substantially constant thickness of liquid medium. In certain embodiments, a barrier between the photobioreactor unit and the body of water upon which the unit is floated facilitates thermal communication between the liquid medium and the body of water.

Claims

1. A method of growing macroalgae in a photobioreactor system comprising:

floating, on a body of water, a longitudinally oriented enclosed photobioreactor section constructed primarily of a substantially flexible material and having a cross-sectional shape, for a cross-section taken essentially perpendicular to a longitudinal axis of the photobioreactor section, that is characterized by at least a portion of its perimeter being curved, when in operation;

introducing a liquid medium comprising macroalgae therein into the photobioreactor segment;

introducing a carbon dioxide-enriched gas into the photobioreactor segment to form a gas headspace; and

moving and reorienting the macroalgae within the liquid medium by mixing the liquid medium,

wherein the moving act involves sparging gas into the liquid medium and wherein the sparging of gas into the liquid medium comprises injecting gas into the liquid medium through periodic gas outlets positioned longitudinally along a horizontal conduit.

2. The method of claim 1 wherein the photobioreactor section comprises an upper channel and a lower channel separated by a substantially horizontal barrier, wherein the upper channel includes the liquid medium.

3. The method of claim 2 wherein the method further comprises flowing cooling water used to remove heat from an industrial process through the lower channel.

4. The method of claim 1 wherein the photobioreactor section is configured to permit the transfer of heat from the body of water to the liquid medium contained in the photobioreactor section and the method further comprises transferring waste heat produced by an industrial process to the body of water, thereby heating the water in the body of water and the liquid medium contained in the photobioreactor section.

5. The method of claim 4 wherein the photobioreactor section comprises a barrier film having a thickness of less than about 5 mm across which the heat is transferred between the body of water and the liquid medium.

6. The method of claim 1 wherein controlling a depth variation of the liquid medium in the photobioreactor section by controlling an operating pressure of the photobioreactor section.

7. The method of claim 1 wherein floating the photobioreactor section on the body of water comprises floating the photobioreactor section such that it has no physical attachment to any other object for at least some portion of the time that the photobioreactor section is floating.

8. The method of claim 1 wherein the substantially flexible material comprises a barrier film having a thickness of less than about 5 mm.

9. The method of claim 8 wherein the method further comprises introducing the liquid medium in the photobioreactor section to form a liquid medium layer of substantially uniform depth therein.

10. A method of generating biomass comprising:

providing a plurality of photobioreactor units constructed primarily of substantially flexible material;

introducing liquid medium comprising phototrophic organisms therein into each of the photobioreactor units to form a liquid medium layer of substantially uniform depth in each of the photobioreactor units;

sealing the photobioreactor units; and

floating the photobioreactor units on a body of water;

wherein the photobioreactor units comprise an upper channel and a lower channel separated by a substantially horizontal barrier, wherein the upper channel includes the liquid medium, and wherein the method further comprises flowing cooling water used to remove heat from an industrial process through the lower channel, the industrial process being external to the photobioreactor units.

11. The method of claim 10 further comprising introducing a carbon dioxide-enriched gas into the upper channel of each of the photobioreactor units to form a gas headspace therein.

12. The method of claim 11 wherein introducing the carbon dioxide-enriched gas comprises sparging the carbon dioxide-enriched gas into the liquid medium.

13. The method of claim 10 wherein the barrier has a thickness of less than about 5 mm.

14. A method of producing biomass, the method comprising:

floating an enclosed photobioreactor on a body of water, the photobioreactor being configured to permit the transfer of heat between liquid medium contained in the photobioreactor and the body of water; and

transferring waste heat produced by an industrial process to the body of water, thereby heating the water in the body of water and the liquid medium contained in the photobioreactor;

wherein the photobioreactor comprises a barrier film having a thickness of less than about 5 mm across which the heat is transferred between the liquid medium and the body of water.

15. The method of claim 14 further comprising introducing a carbon dioxide-enriched gas into the photobioreactor to form a gas headspace therein.

16. The method of claim 15 wherein introducing the carbon dioxide-enriched gas comprises sparging the carbon dioxide-enriched gas into the liquid medium.

17. The method of claim 14 wherein the photobioreactor is constructed primarily of substantially flexible material.

18. The method of claim 14 wherein the body of water comprises an industrial pond.

19. The method of claim 14 wherein floating the photobioreactor on the body of water comprises floating the photobioreactor such that it has no physical attachment to any other object for at least some portion of the time that the photobioreactor is floating.

20. A method of generating biomass comprising:

providing a plurality of photobioreactor units constructed primarily of substantially flexible material;

introducing liquid medium comprising phototrophic organisms therein into each of the photobioreactor units to form a liquid medium layer of substantially uniform depth in each of the photobioreactor units;

sealing the photobioreactor units;

floating the photobioreactor units on a body of water; and

controlling a depth variation of the liquid medium in a photobioreactor unit of the plurality of photobioreactor units by controlling an operating pressure of the photobioreactor unit.

21. The method of claim 20 wherein each photobioreactor unit comprises a barrier film having a thickness of less than about 5 mm and the method further comprises transferring heat across the barrier film between the liquid medium and the body of water.

22. The method of claim 20 further comprising transferring waste heat produced by an industrial process to the body of water, thereby heating the water in the body of water and the liquid medium contained in the photobioreactor units.

23. The method of claim 20 wherein the body of water comprises an industrial pond.

24. The method of claim 20 further comprising introducing a gas containing elevated levels of carbon dioxide into each of the photobioreactor units.

25. The method of claim 20 wherein floating the photobioreactor units on the body of water comprises floating the photobioreactor units such that they have no physical attachment to any other object for at least some portion of the time that the photobioreactor is floating.