Solid-state structures with volatile sintering aids, and methods for fabrication and use thereof
US-2024429439-A1 · Dec 26, 2024 · US
US11075404B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11075404-B2 |
| Application number | US-201816232832-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 26, 2018 |
| Priority date | Apr 10, 2009 |
| Publication date | Jul 27, 2021 |
| Grant date | Jul 27, 2021 |
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 for producing a solid electrolyte, comprising: grinding raw materials comprising lithium sulfide and phosphorus sulfide in a hydrocarbon solvent, optionally comprising stirring a slurry comprising the raw materials and the hydrocarbon solvent in a reaction vessel, and optionally, circulating the slurry through a connecting pipe, wherein the method is carried out in an apparatus comprising the grinder, the reaction vessel and the connecting pipe that connects the grinder and the reaction vessel.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a solid electrolyte, the method comprising: grinding raw materials comprising lithium sulfide and phosphorus sulfide in a hydrocarbon solvent. 2. The method according to claim 1 , comprising: the grinding raw materials comprising lithium sulfide and phosphorus sulfide in the hydrocarbon solvent in a grinder, stirring a slurry comprising the raw materials and the hydrocarbon solvent in a reaction vessel, and circulating the slurry through a connecting pipe, wherein the method is carried out in an apparatus comprising the grinder, the reaction vessel and the connecting pipe that connects the grinder and the reaction vessel. 3. The method according to claim 1 , wherein the grinding is carried out with a rotary mill, a swing mill, a vibration mill, or a bead mill. 4. The method according to claim 1 , wherein the hydrocarbon solvent is a saturated hydrocarbon, an unsaturated hydrocarbon or an aromatic hydrocarbon. 5. The method according to claim 1 , wherein the phosphorus sulfide is phosphorus pentasulfide, and a molar ratio of the lithium sulfide to the phosphorus pentasulfide is from 50:50 to 80:20. 6. The method according to claim 4 , wherein the phosphorus sulfide is phosphorus pentasulfide, and a molar ratio of the lithium sulfide to the phosphorus pentasulfide is from 50:50 to 80:20. 7. The method according to claim 2 , wherein the grinder is a rotary mill, a swing mill, a vibration mill, or a bead mill. 8. The method according to claim 2 , wherein the grinder is a bead mill. 9. The method according to claim 8 , wherein the hydrocarbon solvent is an aromatic hydrocarbon. 10. The method according to claim 8 , wherein a reaction temperature in the reaction vessel is from 60° C. to 300° C. 11. The method according to claim 8 , wherein a heat exchanger is provided to the connecting pipe, the heat exchanger cools the slurry discharged from the reaction vessel and then supplies the slurry to the grinder. 12. The method according to claim 9 , wherein a heat exchanger is provided to the connecting pipe, the heat exchanger cools the slurry discharged from the reaction vessel and then supplies the slurry to the grinder. 13. The method according to claim 2 , wherein a grinding temperature in the grinder is 20° C. or more and 90° C. or less. 14. The method according to claim 2 , wherein the hydrocarbon solvent is a saturated hydrocarbon, an unsaturated hydrocarbon or an aromatic hydrocarbon. 15. The method according to claim 2 , wherein the hydrocarbon solvent is an aromatic hydrocarbon. 16. The method according to claim 2 , wherein the phosphorus sulfide is phosphorus pentasulfide. 17. The method according to claim 16 , wherein a molar ratio of the lithium sulfide to the phosphorus pentasulfide is from 50:50 to 80:20. 18. The method according to claim 2 , wherein a reaction temperature in the reaction vessel is from 60° C. to 300° C. 19. The method according to claim 2 , wherein a heat exchanger is provided to the connecting pipe. 20. The method according to claim 19 , wherein the heat exchanger cools the slurry discharged from the reaction vessel and then supplies the slurry to the grinder. 21. The method according to claim 1 , further comprising: stirring a slurry comprising the raw materials and the hydrocarbon solvent.
Chalcogenide glasses, i.e. S, Se or Te glasses · CPC title
by liquid-phase reaction processes · CPC title
Ionic conductors · CPC title
Pretreated ingredients · CPC title
Manufacturing or production processes characterised by the final manufactured product · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.