GRAVITY FLOW TUBULAR PHOTOBIOREACTOR AND PHOTOBIOREACTOR FARM

• US 20130023043A1
• Filed: 02/16/2012
• Published: 01/24/2013
• Est. Priority Date: 08/17/2009
• Status: Abandoned Application

• Current Assignee: Advanced Algae, Inc.
• Original Assignee: Advanced Algae, Inc.
• Inventors: Hinkens, Dale
• Application Number:
  US13/398,585
• Publication Number:
  US 20130023043A1
• Time in Patent Office: Days
• US Class Current: 435/292.1
• 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 23/18 Open ponds; Greenhouse type or underground installations
• CPC Class Codes: C12M 23/22 Transparent or translucent parts glassware for laboratory use B01L3/00
• CPC Class Codes: C12M 23/26 flexible flexible containers for laboratory use B01L3/505
• CPC Class Codes: C12M 23/48 Holding appliances; Racks; Supports holding devices for laboratory apparatus B01L9/00
• CPC Class Codes: C12M 23/58 Reaction vessels connected in series or in parallel combinations of bioreactors with other apparatus, C12M43/00
• CPC Class Codes: C12M 29/00 Means for introduction, extraction or recirculation of materials, e.g. pumps pumps per se F04B
• CPC Class Codes: C12M 29/24 Recirculation of gas

Abstract

A gravity flow photobioreactor core (10) comprised of a support means (3); a tube (5) that continuously runs and curls with declination about a vertical axis to form a stack (7) of levels (9) and having an inlet sparge (11); a gas exchange tank (13) and a central feed pipe (15) with a sparge (17). A gravity flow photobioreactor farm comprised of a bottom tank (19); a pump (21); a plurality of bioreactor cores (10) connected in series at decreasing elevations and a return pipe (23).

Claims

1. A bioreactor farm comprising:

at least first and second bioreactor cores connected in series, each of the first and second bioreactor cores comprising;

a support;

a tube which at a minimum partially passes light there through, is mounted on the support and includes an upper opening, wherein at last a portion of the tube continuously runs and curls with declination about a vertical axis to form a stack of levels with each level encompassing about 360 degrees around the vertical axis where the radial distance between the tube and the vertical axis indexes within the stack so as to enhance the tube'"'"'s exposure to light emanating from above the stack relative to the tube being vertically aligned at a constant radial distance from the axis within the stack;

the tube also comprising a lower opening;

wherein the first bioreactor core is supported at an elevation higher than an elevation of the second bioreactor core.

2. The bioreactor farm according to claim 1 additionally comprising a gas exchange tank that has a mounting to the support at a position that is generally above the stack, is in fluid communication with the upper opening of the tube, has a slurry entry inlet and has an outlet for the elimination of gas.

3. The bioreactor farm according to claim 2 additionally comprising a central feed pipe in fluid communication with the slurry entry inlet of the gas exchange tank.

4. The bioreactor farm according to claim 1, wherein a difference in elevation between the first and second bioreactor cores is sufficient to cause slurry to move down the tube of the first reactor core and up to the upper opening of the tube of the second bioreactor core.

5. The bioreactor farm according to claim 1 additionally comprising a first gas exchange tank supported at a position that is generally above the tube of the first bioreactor core and a second gas exchange tank supported at a position that is generally above the tube of the second bioreactor core, the first gas exchange tank including an upper fill level that is at a vertical position that is higher than a slurry inlet of the second gas exchange tank.

6. The bioreactor farm according to claim 5, wherein the second bioreactor core is configured to prevent a level of liquid slurry in the second gas exchange tank from rising above the slurry inlet of the second gas exchange tank.

7. A bioreactor core comprising:

a first support;

a first annular tube which substantially passes light there through is mounted on the support, the tube including an upper opening and at least a portion of the tube extending downwardly from the upper opening, along an annular path and with declination about a vertical axis to form a stack of a plurality of levels that are in substantially parallel planes that are vertically spaced with a slope of declination lowering each level and in a direction from top to bottom the radial distance between the tube and the vertical axis within the stack increases; and

a first gas exchange tank supported at a position that is generally above the stack, is in fluid communication with the upper opening of the tube, the first gas exchange tank also has a first fluid fill level and a first slurry entry inlet above the first fluid fill level, the first slurry entry inlet being spaced sufficiently above the first fluid fill level such that as slurry entered into the first gas exchange tank through the first slurry entry inlet, the slurry splashes down onto an upper surface of the fluid at the first fluid fill level, thereby enhancing the release of gas from the slurry.

8. The bioreactor core according to claim 7 additionally comprising a central feed pipe in fluid communication with the outlet side of a pump and the slurry entry inlet of the gas exchange tank and a sparge in communication with the central feed pipe for introducing a gas.

9. The bioreactor core according to claim 7, wherein the diameter of the tube is between about 3 inches to about 5 inches.

10. The bioreactor core according to claim 7, wherein the stack has a vertical height of about 10 feet.

11. The bioreactor core according to claim 7, in combination with a second bioreactor core connected to an outlet of the first annular tube, the second bioreactor core including a second gas exchange tank, the second gas exchange tank being supported at a position that is generally above a second stack of the second bioreactor core, the second gas exchange tank comprising a second fluid fill level and a second slurry entry inlet above the second fluid fill level, the second slurry entry inlet being spaced sufficiently above the second fluid fill level such that as slurry entered into the second gas exchange tank through the second slurry entry inlet, the slurry splashes down onto an upper surface of the fluid at the second fluid fill level, thereby enhancing the release of gas from the slurry.

12. The bioreactor core according to claim 11, wherein the second fluid fill level is at a vertical height that is lower than the first fluid fill level.

13. The bioreactor core according to claim 7, wherein the first bioreactor core is configured to prevent a level of liquid slurry in the first gas exchange tank from rising above the first fluid fill level.

14. The bioreactor core according to claim 11, wherein the first bioreactor core is configured to prevent a level of liquid slurry in the first gas exchange tank from rising above the first fluid fill level, and wherein the second bioreactor core is configured to prevent a level of liquid slurry in the second gas exchange tank from rising above the second fluid fill level.