Sustainable, facile separation of the molten carbonate electrolysis cathode product
US-11346013-B2 · May 31, 2022 · US
US11834749B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11834749-B2 |
| Application number | US-202117330101-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 25, 2021 |
| Priority date | Oct 29, 2018 |
| Publication date | Dec 5, 2023 |
| Grant date | Dec 5, 2023 |
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 process for the separation of electrolyte from the carbon in a solid carbon/electrolyte cathode product formed at the cathode during molten carbonate electrolysis. The processes allows for easy separation of the solid carbon product from the electrolyte without any observed detrimental effect on the structure and/or stability of the resulting solid carbon nanomaterial.
Opening claim text (preview).
What is claimed is: 1. A system comprising: an electrolysis chamber; a force applicator configured to press a mixed product including a solid carbon and a molten electrolyte, wherein the force applicator is configured to compress the mixed product in the electrolysis chamber; and a filter configured to isolate the solid carbon from the electrolyte. 2. The system of claim 1 , wherein the filter is configured to be positioned below the mixed product. 3. The system of claim 1 , wherein the filter is configured to be positioned to the side of the mixed product. 4. The system of claim 1 , wherein the filter is configured to be positioned above the mixed product. 5. The system of claim 1 , wherein the filter is configured to be positioned to the backside of the mixed product. 6. The system of claim 1 , wherein the force applicator is configured to apply and remove the pressing force repeatedly. 7. The system of claim 1 , wherein said filter comprises an interface with pores, said interface configured to remove the electrolyte from said solid carbon. 8. The system of claim 7 , further comprising a vacuum configured to remove the electrolyte from said solid carbon. 9. The system of claim 1 , wherein the system is under a gas that is free or substantially free of oxygen. 10. The system of claim 9 , wherein the gas is selected from nitrogen, carbon dioxide, argon, methane, ammonia, hydrogen, hydrogen sulfide, and any combination thereof. 11. The system of claim 1 , wherein the mixed product is cooled after formation by electrolysis, and further comprising a heater configured to reheat the mixed product prior to the force applicator pressing the mixed product. 12. The system of claim 1 , further comprising: a cathode configured to be positioned in the electrolysis chamber; and an extraction chamber, wherein the mixed product is configured to be moved from the cathode to the extraction chamber prior to said force applicator pressing the mixed product. 13. The system of claim 1 , wherein the electrolyte is not a flowing electrolyte. 14. The system of claim 1 , wherein the system does not include a recirculation loop that recirculates the electrolyte. 15. The system of claim 1 , wherein the solid carbon has an average thickness greater than 1 millimeter. 16. The system of claim 1 , wherein the solid carbon comprises greater than about 80% carbon nano-materials. 17. The system of claim 1 , wherein the solid carbon comprises nano-fibers, nano-tubes, nano-onions, nano-platelets, or nano-scaffolds. 18. The system of claim 1 , wherein the solid carbon comprises graphene nano-materials. 19. The system of claim 1 , wherein the solid carbon is formed from raw carbon nano-material that agglomerates during a carbonate electrolysis, and said filter has pores larger than the raw carbon nano-material. 20. The system of claim 1 , wherein the solid carbon comprises a paste. 21. The system of claim 1 , further comprising an electrolysis chamber collecting electrolyte that passes through the filter. 22. The system of claim 1 , wherein the filter is configured to be positioned either below, above, to the side, above, or the backside of the mixed product, or a combination thereof. 23. The system of claim 1 , wherein the force applicator is configured to press the mixed product by applying a compression force, torque, a rotational force, a twisting force or any combination thereof.
Supplying or removing reactants or electrolytes; Regeneration of electrolytes · CPC title
for discharging filtrate · CPC title
Filters adapted for location in special places, e.g. pipe-lines, pumps, stop-cocks, (B01D35/05 takes precedence; {water pipe system filters E03B3/18, E03B7/07; dirt catchers in sewers E03F; filters or strainers for pipe-lines in general B08B, E03F; object or dirt catching devices in sinks or the like E03C1/26; suction strainers or filters for pumps F04B53/005, F04D29/70}) · CPC title
co-operating with permeable casings or strainers · CPC title
Nano-sized carbon materials · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.