Solid-state structures with volatile sintering aids, and methods for fabrication and use thereof
US-2024429439-A1 · Dec 26, 2024 · US
US2024336480A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2024336480-A1 |
| Application number | US-202318529132-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 5, 2023 |
| Priority date | Apr 7, 2023 |
| Publication date | Oct 10, 2024 |
| Grant date | — |
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The present disclosure relates to a method of producing a solid electrolyte with a uniform particle size distribution and a spherical shape. The method includes preparing a raw material comprising one or more of a lithium (Li) element, a phosphorus (P) element, or a sulfur(S) element, preparing a starting material comprising the raw material and a solvent, obtaining an intermediate in powder form by spray drying the starting material, and obtaining a sulfide-based solid electrolyte by heat treating the intermediate.
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What is claimed is: 1 . A method of producing a solid electrolyte, the method comprising: preparing a raw material comprising one or more of a lithium (Li) element, a phosphorus (P) element, or a sulfur(S) element; preparing a starting material comprising the raw material and a solvent; obtaining an intermediate in powder form by spray drying the starting material; and obtaining a sulfide-based solid electrolyte by heat treating the intermediate. 2 . The method of claim 1 , wherein the raw material includes Li 2 S and P 2 S 5 . 3 . The method of claim 1 , wherein the raw material further comprises a lithium compound comprising a halogen element. 4 . The method of claim 1 , wherein the solvent comprises tetrahydrofuran (THF). 5 . The method of claim 1 , wherein the starting material has a solid content in an amount of 10% by weight to 30% by weight. 6 . The method of claim 1 , wherein the obtaining of the intermediate comprises spraying the starting material into a chamber of a spray dryer through a nozzle atomizer. 7 . The method of claim 6 , wherein an evaporation quantity of the chamber ranges from 1 kg/hr to 4 kg/hr. 8 . The method of claim 6 , wherein the starting material is sprayed into the chamber at a spray rate of 50 ml/min to 70 ml/min. 9 . The method of claim 6 , wherein an internal pressure of the chamber ranges from 1.3 atm to 1.5 atm. 10 . The method of claim 6 , wherein the spray dryer comprises: a chamber defining an internal space of a preset size; a nozzle atomizer connected to the chamber and configured to spray the starting material; a first compressor connected to the nozzle atomizer and configured to supply a carrier gas; a second compressor connected to the chamber and configured to supply a gas to thereby adjust an internal pressure of the chamber; a sensor mounted in the chamber and configured to measure the internal pressure of the chamber; a vent valve configured to discharge the carrier gas in the chamber to an outside of the chamber; and a controller connected to the second compressor and the vent valve and configured to control whether to operate the second compressor and the vent valve based on the internal pressure of the chamber measured by the sensor. 11 . The method of claim 1 , wherein the obtaining of the intermediate is performed in a temperature of 180° C. to 240° C. 12 . The method of claim 1 , wherein the obtaining of the intermediate comprises spray drying the starting material for 1 second to 5 seconds. 13 . The method of claim 1 , wherein the obtaining of the sulfide-based solid electrolyte comprises heat treating the intermediate in a temperature of 300° C. to 500° C. for 12 hours to 48 hours. 14 . The method of claim 1 , wherein D50 of the sulfide-based solid electrolyte ranges from 5 μm to 10 μm. 15 . The method of claim 1 , wherein (D90-D10)/D50 of the sulfide-based solid electrolyte ranges from 1 to 3. 16 . The method of claim 1 , wherein a tap density of the sulfide-based solid electrolyte ranges from 0.5 g/ml to 0.7 g/ml. 17 . The method of claim 1 , wherein a pellet density of the sulfide-based solid electrolyte ranges from 1.65 g/ml to 1.8 g/ml.
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