Garnet materials for li secondary batteries and methods of making and using garnet materials
US-2015099188-A1 · Apr 9, 2015 · US
US10566654B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10566654-B2 |
| Application number | US-201615758345-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 27, 2016 |
| Priority date | Oct 9, 2015 |
| Publication date | Feb 18, 2020 |
| Grant date | Feb 18, 2020 |
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A method for preparing electrolyte material having a NASICON structure, based on a Na 3+x Sc x Zr 2−x (SiO 4 ) 2 (PO 4 ) compound where 0≤x<2. The method includes providing an acidic, aqueous solution which, according to a desired stoichiometry, comprises sodium, scandium and zirconium in the form of water-soluble nitrates, acetates or carbonates, and soluble silicates or orthosilicic acids or organic silicon compounds in dissolved form; subsequently adding phosphoric acid or ammonium dihydrogenphosphate or other soluble phosphates, according to the desired stoichiometry, complex zirconium dioxide phosphates forming as colloidal precipitations; and subsequently drying and calcining the mixture.
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The invention claimed is: 1. A method for preparing electrolyte material having a NASICON structure, based on a Na 3 Zr 2 (SiO 4 ) z (PO 4 ) 3 compound where 0≤x<2, comprising the steps of: providing an acidic, aqueous solution which, according to a desired stoichiometry, comprises sodium, scandium and zirconium in the form of water-soluble nitrates, acetates or carbonates, and soluble silicates or orthosilicic acids or organic silicon compounds in dissolved form as starting materials; subsequently adding phosphoric acid or ammonium dihydrogenphosphate or other soluble phosphates, according to the desired stoichiometry, thereby forming a mixture having complex zirconium dioxide phosphates as colloidal precipitations; and subsequently drying and calcining the mixture. 2. The method according to claim 1 , wherein the starting materials are selected according to the stoichiometry for 0≤x<2. 3. The method according to claim 1 , wherein the mixture is dried at temperatures of between 60° C. and 120° C. 4. The method according to claim 1 , wherein the mixture is calcined at temperatures of between 700° C. and 900° C. 5. The method according to claim 1 , wherein, the dried and calcined mixture comprises particles having a particle size, determined using a scanning electron microscope, of approximately 0.1 μm. 6. The method according to claim 1 , wherein the dried and calcined mixture is subsequently ground. 7. The method according to claim 6 , wherein the dried, calcined and ground mixture is subsequently compressed. 8. The method according to claim 7 , wherein the dried, calcined and ground mixture is compressed at pressures of between 50 and 100 MPa. 9. The method according to claim 7 , wherein the compressed mixture is sintered at temperatures of between 1200° and 1300° C. 10. A sodium ion-conducting membrane comprising a Na 3 Zr 2 (SiO 4 ) z (PO 4 ) 3 compound where 0.3≤x≤0.6, which can be prepared according to claim 1 , having an ionic conductivity of more than 1.2·10 −3 S/cm at 25° C. 11. A sodium ion-conducting membrane according to claim 10 , having a density of more than 90% of a theoretical density. 12. A sodium ion-conducting membrane comprising a Na 3 Zr 2 (SiO 4 ) z (PO 4 ) 3 compound where 0.3≤x≤0.6, which can be prepared according to claim 1 , having an ionic conductivity of more than 3·10 −3 S/cm at 25° C. 13. A sodium ion-conducting membrane according to claim 12 , having a density of more than 90% of a theoretical density.
Alkali metal silicates ({C01B33/24} , C01B33/26 take precedence) · CPC title
Pressure sintering · CPC title
Alkali metal oxides or oxide-forming salts thereof · CPC title
Phosphates (perphosphates C01B15/16) · CPC title
of accumulators having only flat construction elements, i.e. flat positive electrodes, flat negative electrodes and flat separators · CPC title
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