Highly Efficient Enzymatic Bioanodes and Biocathodes
US-2015364784-A1 · Dec 17, 2015 · US
US9755261B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9755261-B2 |
| Application number | US-201514843303-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 2, 2015 |
| Priority date | Sep 2, 2015 |
| Publication date | Sep 5, 2017 |
| Grant date | Sep 5, 2017 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
The present invention provides a novel method that recovers metal components from sulfide mineral tailings by Microbial Fuel Cell. The traditional bio-hydrometallurgy reaction is split to one oxidization reaction taking place in the anode chamber and one reduction reaction taking place in the cathode chamber. H + generated during the oxidization reaction is continually transferred to cathode chamber through proton exchange membrane and reacted with O 2 to generate H 2 O, which not only increases the reaction rate in anode chamber but also decreases equipment corrosion caused by excessive H + . The method of the present invention, recovering metals as well as electronic power, is environment-friendly.
Opening claim text (preview).
What is claimed is: 1. A method for recovering metal iron from sulfide mineral tailings, comprising adding said sulfide mineral tailings to a Double-chambered Microbial Fuel Cell (MFC) and producing free iron with a high recovering rate, wherein said Double-chambered Microbial Fuel Cell comprises a cathode and an anode chamber separated by a proton exchange membrane, and electrodes in said anode and said cathode chambers connected through an external circuit; wherein said anode chamber contains said sulfide mineral tailings, an electrode and an electricigens culture comprising Sulfur-Oxidizing bacteria and Acidithiobacillus ferrooxidans ; wherein initial pH of said anode chamber is 1.5˜2.5 and anaerobic condition is maintained in said anode chamber; wherein said cathode chamber contains a phosphate buffer, an electrode and an aerator; and wherein the reaction in said Double-chambered MFC is depicted with equations below: FeS+6Fe 3+ +0.5O 2 +3H 2 O→7Fe 2+ +SO 4 2− +6H + anode: FeS+6Fe 3+ +4H 2 O →7Fe 2+ +8H + +SO 4 2− +2e − cathode: 2.25O 2 +9H + +9e − →4.5H 2 O or FeS+2O 2 →Fe 2+ +SO 4 2− anode: FeS+4H 2 O →Fe 2+ +SO 4 2− +8H + +8e − cathode: 2O 2 +8H + +8e − →4H 2 O 2. The method of claim 1 , wherein said electrodes in said cathode and said anode chamber are made of graphite felt or carbon cloth. 3. The method of claim 1 , wherein said anode chamber contains 5˜50 g/L sulfide mineral tailings. 4. The method of claim 1 , wherein said phosphate buffer in said cathode chamber contains 50 mM phosphate salt (pH 7.0). 5. A Double-chambered Microbial Fuel Cell device for recovering iron metal from sulfide mineral tailings, comprising a cathode and an anode chamber separated by a proton exchange membrane, and electrodes in said anode and said cathode chamber connected through an external circuit, wherein said anode chamber contains said sulfide mineral tailings, an electrode and an electricigens culture comprising Sulfur-Oxidizing bacteria and Acidithiobacillus ferrooxidans ; wherein initial pH of said anode chamber is 1.5˜2.5 and anaerobic condition is maintained in said anode chamber; wherein said cathode chamber contains a phosphate buffer, an electrode and an aerator; and wherein the reaction in said Double-chambered MFC is depicted with equations below: FeS+6Fe 3+ +0.5O 2 +3H 2 O→7Fe 2+ +SO 4 2− +6H + anode: FeS+6Fe 3+ +4H 2 O →7Fe 2+ +8H + +SO 4 2− +2e − cathode: 2.25O 2 +9H + +9e − →4.5H 2 O or FeS+2O 2 →Fe 2+ +SO 4 2− anode: FeS+4H 2 O→Fe 2+ +SO 4 2− +8H + +8e − cathode: 2O 2 +8H + +8e −→ 4H 2 O
Biochemical fuel cells, i.e. cells in which microorganisms function as catalysts · CPC title
Recycling · CPC title
Fuel cells with polymeric electrolytes · CPC title
Fuel cells · CPC title
with the aid of microorganisms or enzymes, e.g. bacteria or algae · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.