초록 ▼

Embodiments may include efficient fuel cell systems including an anode, a cathode, a lead-containing cathode catalyst, at least one proton exchange connector, and perhaps even an external circuit between the anode and the cathode. Other embodiments may include enhanced degradation of contaminants in

Embodiments may include efficient fuel cell systems including an anode, a cathode, a lead-containing cathode catalyst, at least one proton exchange connector, and perhaps even an external circuit between the anode and the cathode. Other embodiments may include enhanced degradation of contaminants in environmental media such as perhaps petroleum hydrocarbon in groundwater with microbial fuel cells and the like.

대표청구항 ▼

What is claimed is: 1. A method of multi-purpose in-situ microbial fuel cell functions for waste remediation and energy generation comprising the steps of: creating an in-situ closed anaerobic anode chamber within an in-situ environmental media having at least one contaminant selected from a group

What is claimed is: 1. A method of multi-purpose in-situ microbial fuel cell functions for waste remediation and energy generation comprising the steps of: creating an in-situ closed anaerobic anode chamber within an in-situ environmental media having at least one contaminant selected from a group consisting of a petroleum contaminant and a refined petroleum contaminant; providing at least one microbial population in said in-situ closed anaerobic anode chamber; metabolizing said at least one contaminant in said in-situ environmental media with said at least one microbial population to generate electrons and protons in said in-situ closed anaerobic anode chamber; remediatingly biodegrading at least some of said at least one contaminant; extracting electrons from said in-situ closed anaerobic anode chamber with at least one anode in said in-situ closed anaerobic anode chamber; transferring said electrons from said in-situ closed anaerobic anode chamber to an in-situ open cathode chamber through an external circuit, wherein said in-situ open cathode chamber is located at or near a surface of said in-situ environmental media; generating electrical power from said transfer of said electrons from said in-situ closed anaerobic anode chamber to said in-situ open cathode chamber; transferring protons from said in-situ closed anaerobic anode chamber to said in-situ open cathode chamber with a proton exchange connector between said at least one anode to at least one cathode of said in-situ open cathode chamber; and reacting oxygen with said protons in said in-situ open cathode chamber to create by-products. 2. The method according to claim 1 wherein said environmental media is selected from a group consisting of an underground environment, a saturated subsurface, unsaturated subsurface, soil, groundwater, sediment, surface water, and petroleum-impacted saturated soils. 3. The method according to claim 1 wherein said petroleum contaminant is selected from a group of petroleum subsurface contaminants, petroleum hydrocarbons, and petroleum compounds. 4. The method according to claim 1 wherein said refined petroleum contaminant is selected from a group consisting of refined petroleum subsurface contaminants, refined petroleum hydrocarbons, refined petroleum compounds, diesel, diesel range organic compounds, and gasoline. 5. The method according to claim 1 wherein said in-situ closed anaerobic anode chamber is located underground in said in-situ environmental media. 6. The method according to claim 1 and further comprising the step of driving an electrical current through said external circuit with a lead-containing cathode catalyst in said in-situ open cathode chamber. 7. The method according to claim 6 wherein said step of driving said electrical current through said external circuit with said lead-containing cathode catalyst comprises the step of driving said electrical current through said external circuit with a lead dioxide cathode catalyst in said in-situ open cathode chamber. 8. The method according to claim 1 and further comprising the step of driving an electrical current through said external circuit with a platinum-containing cathode catalyst in said in-situ open cathode chamber. 9. The method according to claim 1 and further comprising the step of driving an electrical current through said external circuit with a manganese-containing cathode catalyst in said in-situ open cathode chamber. 10. The method according to claim 1 wherein said at least one microbial population is selected from a group consisting of iron-reducing bacteria, denitrifying bacteria populations, sulfate-reducing bacteria populations, methanogenic bacteria, fermenting bacteria, Citrobacter sp., Pseudomonas sp., Strehotrophomonas sp., Shewanella sp. ANA-3, Alishewanella sp., γ-Proteobacteria, Citramonas sp., Desulfovibrio sp., and Dechloromonas. 11. The method according to claim 10 and further comprising the step of forming a biofilm of said at least one microbial population on said at least one anode of said in-situ closed anaerobic anode chamber. 12. The method according to claim 1 wherein said step of remediatingly biodegrading at least some of said at least one contaminant comprises the step of reducing said at least one contaminant by a reduction selected from a group consisting of: about 50%; about 55%; about 60%; about 65%; about 70%; about 75%; about 80%; about 85%; about 90%; about 95%; and between about 50% and about 95%. 13. The method according to claim 1 wherein said proton exchange connector comprises a conductive liquid medium. 14. The method according to claim 1 wherein said proton exchange connector comprise a proton exchange membrane. 15. The method according to claim 1 wherein said proton exchange connector comprise at least one proton bridge. 16. The method according to claim 1 wherein said step of transferring said protons from said in-situ closed anaerobic anode chamber to said in-situ open cathode chamber with said proton exchange connector comprises the step of transferring said protons from said in-situ closed anaerobic anode chamber to said in-situ open cathode chamber with a network of proton bridges between multiple anodes and said in-situ open cathode chamber. 17. The method according to claim 1 and further comprising the step of accepting said transferred electrons from said in-situ closed anaerobic anode chamber with at least one electron acceptor in said in-situ open cathode chamber, said electron acceptor is selected from a group consisting of permanganate, uranium, oxygen, oxygen-releasing compounds, peroxide, halogenated compounds, oxidants of permanganate, percabonate, cynide, selenium, persulfate, ozone, sulfate, nitrate, iron, manganese, arsenate, selenate, and chromate. 18. The method according to claim 1 wherein said step of reacting oxygen with said protons in said in-situ open cathode chamber comprises the step of producing water. 19. The method according to claim 1 wherein said step of reacting oxygen with said protons in said in-situ open cathode chamber comprises the step of reacting oxygen from ambient air with said protons in said in-situ open cathode chamber. 20. The method according to claim 1 wherein said step of reacting oxygen with said protons in said in-situ open cathode chamber comprises the step of reacting oxygen from oxygen releasing compounds with said protons in said in-situ open cathode chamber. 21. The method according to claim 1 wherein said oxygen releasing compounds are selected from a group consisting of permanganate and peroxide.