PLASTIC DISPOSABLE REACTOR SYSTEM

• US 20100184177A1
• Filed: 01/22/2010
• Published: 07/22/2010
• Est. Priority Date: 01/22/2009
• Status: Abandoned Application

• Current Assignee: Energetix LLC
• Original Assignee: Energetix LLC
• Inventors: MITCHELL, ANDREW G.
• Application Number:
  US12/692,038
• Publication Number:
  US 20100184177A1
• Time in Patent Office: Days
• US Class Current: 435/166
• CPC Class Codes: C12M 21/02 Photobioreactors culturing algae A01G33/00, A01H4/001, C12N1/12
• CPC Class Codes: C12M 23/28 disposable or single use
• CPC Class Codes: C12M 43/04 Bioreactors or fermenters combined with combustion devices or plants, e.g. for carbon dioxide removal C12M43/06 takes precedence; recovery of carbon dioxide C12F3/02
• CPC Class Codes: C12M 47/18 Gas cleaning, e.g. scrubbers; Separation of different gases separating dispersed particles from gases or vapours B01D45/00; separation of gases or vapours B01D53/00; gas washing apparatus for laboratory uses B01L5/04
• CPC Class Codes: Y02P 20/59 Biological synthesis; Biological purification

Abstract

A plastic, disposable reactor (“PDR”) system is presented that will allow growth of microorganisms at various temperatures and pressures cost effectively. In this invention, the use of the system for aquaculture of algae is presented. The use of the reactor will allow carbon sequestration and significant production of a renewable energy source. The incorporation of recycled materials in various components of the plant also benefits the environment.

Claims

1. A method for processing biogas, wherein the biogas contains carbon dioxide, the method comprising the steps of:

providing a reactor train, wherein the reactor train comprises at least two cylindrical plastic tanks, wherein the tanks contain algae;

dissolving the carbon dioxide into water;

moving the carbon dioxide saturated water through multiple valves, wherein at least one of the valves is operatively connected to a fluid conveying pipe, wherein the pipe is operatively connected to the plastic tanks; and

,

converting the carbon dioxide to organic molecules and oxygen by moving the carbon dioxide saturated water through the algae.

2. The method of claim 1, wherein the method further comprises the steps of:

providing at least a second reactor train, the second reactor train comprising at least two cylindrical plastic tanks, the second reactor train having a top fluid conveying pipe and a bottom fluid conveying pipe;

drawing algae and water from the bottom pipe through the tanks; and

,

when at least approximately one half of the algae has been drawn into the tanks, reconfiguring at least two valves to draw additional carbon dioxide saturated water through the tanks; and

,

converting the carbon dioxide to organic molecules and oxygen.

3. The method of claim 1, wherein the method further comprises the steps of:

cleaning the interior of the tanks with a bleaching agent and water; and

,

placing algae in the cleaned tanks.

4. The method of claim 2, wherein the method further comprises the steps of:

cleaning the interior of the tanks with a bleaching agent and water; and

,

placing algae in the cleaned tanks.

5. The method of claim 3, wherein the tanks are made of a material chosen from the group comprising:

polyethylene teraphthalate, clear polyvinyl chloride, polypropylene, polyethylene, high density polyethylene, cross-linked polyethylene, and clear polycarbonate.

6. The method of claim 4, wherein the tanks are made of a material chosen from the group comprising:

polyethylene teraphthalate, clear polyvinyl chloride, polypropylene, polyethylene, high density polyethylene, cross-linked polyethylene, and clear polycarbonate.

7. The method of claim 6, wherein the tanks are made of polyethylene teraphthalate.

8. The method of claim 7, wherein the water is preheated to between about 24°

C. and about 32°

C., wherein the carbon dioxide saturated water is moved through the algae at a linear velocity of between approximately 0 m/s to approximately 0.01 m/s.

9. A plastic reactor system, wherein the system comprises:

a gas-liquid contacting device;

a top fluid conveying pipe;

a bottom fluid conveying pipe; and

,

at least two plastic tanks, the tanks being operatively attached to the conveying pipes, the tanks containing algae.

10. The system of claim 9, wherein the tanks are made of a material chosen from the group comprising:

polyethylene teraphthalate, clear polyvinyl chloride, polypropylene, polyethylene, high density polyethylene, cross-linked polyethylene, and clear polycarbonate.

11. The system of claim 9, wherein the system further comprises:

at least a second reactor train, the second reactor train comprising at least two cylindrical plastic tanks, the second reactor train having a top fluid conveying pipe and a bottom fluid conveying pipe.

12. The system of claim 10, wherein the system further comprises:

at least a second reactor train, the second reactor train comprising at least two cylindrical plastic tanks, the second reactor train having a top fluid conveying pipe and a bottom fluid conveying pipe.

13. The system of claim 11, wherein the tanks comprise:

a filter; and

,

a connection device comprising a male to male connector with a tube insert welded to the connector and attached to a plug of porous plastic material of diameter less than a nominal thread diameter of the connector.

14. The system of claim 12, wherein the tanks comprise:

a filter; and

,

a connection device comprising a male to male connector with a tube insert welded to the connector and attached to a plug of porous plastic material of diameter less than a nominal thread diameter of the connector.

15. The system of claim 13, wherein the tanks have an internal diameter, a height, and a wall thickness, wherein the system further comprises:

the internal diameter is between about 0 and about 5 inches, the height is between about 0 and about 24 feet, and the wall thickness is between about 0 and about ¼

inch.

16. The system of claim 14, wherein the tanks have an internal diameter, a height, and a wall thickness, wherein the system further comprises:

the internal diameter is between about 0 and about 5 inches, the height is between about 0 and about 24 feet, and the wall thickness is between about 0 and about ¼

inch.

17. The system of claim 13, wherein the tanks have an internal diameter, a height, and a wall thickness, wherein the system further comprises:

the internal diameter is greater than about 5 inches, the height is greater than about 24 feet, and the wall thickness is greater than about ¼

inch.

18. The system of claim 14, wherein the tanks have an internal diameter, a height, and a wall thickness, wherein the system further comprises:

the internal diameter is greater than about 5 inches, the height is greater than about 24 feet, and the wall thickness is greater than about ¼

inch.

19. A method for processing biogas, wherein the biogas contains carbon dioxide, the method comprising the steps of:

providing a reactor train, wherein the reactor train comprises at least two cylindrical plastic tanks, wherein the tanks contain algae;

dissolving the carbon dioxide into a liquid media;

moving the carbon dioxide saturated liquid media through multiple valves, wherein at least one of the valves is operatively connected to fluid conveying pipe, wherein the pipe is operatively connected to the plastic tanks; and

,

converting the carbon dioxide to organic molecules and oxygen by moving the carbon dioxide saturated liquid media through the algae.

20. The method of claim 19, wherein the method further comprises the step of:

extracting an oxygen enriched stream.