Integrated solvent deasphalting, hydrotreating and steam pyrolysis process for direct processing of a crude oil
US-9284502-B2 · Mar 15, 2016 · US
US11495814B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11495814-B2 |
| Application number | US-202016934779-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 21, 2020 |
| Priority date | Jun 17, 2020 |
| Publication date | Nov 8, 2022 |
| Grant date | Nov 8, 2022 |
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.
A method and systems are provided for utilizing black powder to form an electrolyte for a flow battery. In an exemplary method the black powder is heated under an inert atmosphere to form Fe 3 O 4 . The Fe 3 O 4 is dissolved in an acid solution to form an electrolyte solution. A ratio of iron (II) to iron (III) is adjusted by a redox process.
Opening claim text (preview).
What is claimed is: 1. A method for forming electrolyte solutions for a flow battery from black powder, wherein the black powder comprises Fe 3 O 4 , Fe 2 O 3 , or FeOOH, or any combination thereof, the method comprising: heating the black powder under an inert atmosphere to form Fe 3 O 4 ; dissolving the Fe 3 O 4 in an acid solution to form an electrolyte solution; and adjusting a ratio of iron (II) to iron (III) by a redox process. 2. The method of claim 1 , comprising analyzing the black powder for naturally occurring radioactive materials. 3. The method of claim 2 , comprising discarding black powder comprising naturally occurring radioactive materials. 4. The method of claim 1 , comprising heating the black powder to a temperature of between about 400° C. and about 700° C. 5. The method of claim 1 , comprising heating the black powder to a temperature of about 400° C. 6. The method of claim 1 , comprising mixing the acid solution to a concentration of about 1 molar to about 6 molar. 7. The method of claim 1 , comprising mixing an HCl solution to a concentration of about 1 molar to about 6 molar to form the acid solution. 8. The method of claim 1 , comprising dissolving the Fe 3 O 4 in an acid solution comprising an HCl solution to form the electrolyte solution of a concentration of about 1 molar to about 4 molar iron ions. 9. The method of claim 1 , comprising adjusting the ratio of iron (II) to iron (III) by reducing iron (III) to iron (II) in an electrochemical cell. 10. The method of claim 9 , comprising adjusting the ratio of iron (III) to iron (II) in the flow battery during a recharging process. 11. The method of claim 1 , comprising dissolving a vanadium compound in an acid to form an anolyte. 12. The method of claim 11 , comprising dissolving VCl 3 , VOSO 4 , or both in an HCl solution form a solution of about 1 M to about 4 M in concentration of vanadium.
by recharging of redox couples containing fluids; Redox flow type batteries · CPC title
Fuel cells · CPC title
Ferroso-ferric oxide [Fe3O4] · CPC title
Acid electrolytes · CPC title
characterised by the electrolyte material (H01M8/12 takes precedence) · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.