Diluting exhaust gas being supplied to bioreactor

• US 8,889,400 B2
• Filed: 05/20/2010
• Issued: 11/18/2014
• Est. Priority Date: 05/20/2010
• Status: Active Grant

• Current Assignee: Pond Technologies, Inc. (Pond Technologies Holdings, Inc.)
• Original Assignee: Pond Biofuels, Inc.
• Inventors: Martin, Steven C., Kolesnik, Max, Gonzalez, Jaime A.
• Primary Examiner(s): Fox, Allison
• Assistant Examiner(s): Pyla, Yvonne
• Application Number:
  US12/784,126
• Publication Number:
  US 20110287525A1
• Time in Patent Office: 1,643 Days
• Field of Search: None
• 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 43/06 Photobioreactors combined with devices or plants for gas production different from a bioreactor of fermenter
• CPC Class Codes: C12N 1/12 Unicellular algae; Culture media therefor as new plants A01H13/00
• CPC Class Codes: C12N 13/00 Treatment of microorganisms or enzymes with electrical or wave energy, e.g. magnetism, sonic waves
• CPC Class Codes: Y02E 50/10 Biofuels, e.g. bio-diesel
• CPC Class Codes: Y02E 50/30 Fuel from waste, e.g. synthetic alcohol or diesel

Abstract

There is provided a process of growing a phototrophic biomass in a reaction zone. Prior to supplying a reaction zone feed material, including gaseous exhaust from a gaseous exhaust material producing process, supplying the reaction zone feed material with a supplemental gaseous dilution agent, wherein the carbon dioxide concentration of the supplemental gaseous dilution agent is less than the carbon dioxide concentration of the gaseous exhaust material which is supplied to the reaction zone feed material.

Claims

1. A process of growing a phototrophic biomass in a reaction zone, wherein the reaction zone includes an operative reaction mixture, wherein the operative reaction mixture includes the phototrophic biomass disposed in an aqueous medium, comprising:

producing gaseous exhaust material with a gaseous exhaust material producing process, wherein the gaseous exhaust material includes carbon dioxide;

supplying a supplemental gaseous dilution agent to the gaseous exhaust material to produce a diluted gaseous exhaust material, wherein the supplemental gaseous dilution agent has a carbon dioxide concentration that is less than the carbon dioxide concentration of the gaseous exhaust material and wherein the supplying of the supplemental gaseous dilution agent to the gaseous exhaust material is effected in response to sensing of a carbon dioxide concentration in the gaseous exhaust material being discharged from the carbon dioxide producing process which is greater than a predetermined maximum carbon dioxide concentration value;

supplying the diluted gaseous exhaust material to the reaction zone such that carbon dioxide is received by the phototrophic biomass so as to provide a carbon dioxide-enriched phototrophic biomass in the aqueous medium; and

exposing the carbon dioxide-enriched phototrophic biomass disposed in the aqueous medium to photosynthetically active light radiation so as to effect photosynthesis.

2. The process as claimed in claim 1;

wherein the supplying of the supplemental gaseous dilution agent to the gaseous exhaust material provides a carbon dioxide concentration in the diluted gaseous exhaust material being supplied to the reaction zone which is below a predetermined maximum carbon dioxide concentration value.

3. The process as claimed in claim 1;

wherein the supplying of the supplemental gaseous dilution agent to the gaseous exhaust material effects dilution of the gaseous exhaust material with respect to carbon dioxide concentration.

4. The process as claimed in claim 1;

wherein the supplying of the supplemental gaseous dilution agent to the gaseous exhaust material effects a reduction of the carbon dioxide concentration of the gaseous exhaust material.

5. The process as claimed in claim 1;

wherein the gaseous exhaust material includes an upstream gaseous exhaust material and a downstream gaseous exhaust material, wherein the downstream gaseous exhaust material is downstream of the upstream gaseous exhaust material relative to the reaction zone;

and wherein the supplemental gaseous dilution agent is admixed with the upstream gaseous exhaust material to provide the downstream gaseous exhaust material such that the concentration of carbon dioxide in the downstream gaseous exhaust material is less than the concentration of carbon dioxide in the upstream gaseous exhaust material.

6. The process as claimed in claim 1;

wherein the supplying of the gaseous exhaust material with a supplemental gaseous dilution agent is effected while the gaseous exhaust material is being produced by the gaseous exhaust material producing process.

7. The process as claimed in claim 1;

wherein the supplying of the gaseous exhaust material with a supplemental gaseous dilution agent is effected while the gaseous exhaust material is being supplied to the reaction zone.

8. The process as claimed in claim 1;

wherein the exposing of the carbon dioxide-enriched phototrophic biomass disposed in the aqueous medium to photosynthetically active light radiation is effected while the supplying of the gaseous exhaust material with a supplemental gaseous dilution agent is being effected.

9. The process as claimed in claim 1;

wherein the supplemental gaseous dilution agent is gaseous material.

10. The process as claimed in claim 1;

wherein the supplemental gaseous dilution agent includes air.

11. The process as claimed in claim 1;

wherein the gaseous exhaust material is being supplied to the reaction zone as a flow; and

wherein the supplemental gaseous dilution agent is being supplied to the gaseous exhaust material as a flow.

12. The process as claimed in claim 1;

wherein the supplying of the supplemental gaseous dilution agent is effected while the gaseous exhaust material is being produced by the gaseous exhaust material producing process.

13. The process as claimed in claim 1;

wherein the supplying of the supplemental gaseous dilution agent is effected while the diluted gaseous exhaust material is being supplied to the reaction zone.

14. The process as claimed in claim 13;

wherein the exposing of the carbon dioxide-enriched phototrophic biomass disposed in the aqueous medium to photosynthetically active light radiation is effected while the supplying of the supplemental gaseous dilution agent is being effected.