Method for manufacturing non-aqueous secondary battery electrode
US-2024332484-A1 · Oct 3, 2024 · US
US10312500B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10312500-B2 |
| Application number | US-201614988917-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 6, 2016 |
| Priority date | Jan 6, 2016 |
| Publication date | Jun 4, 2019 |
| Grant date | Jun 4, 2019 |
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A high density slurry comprising encapsulated sulfur particles, carbon nanofibers and activated carbon black suitable for use in forming the active material of an electrode. A method for forming the high density sulfur slurry is also provided. A cathode containing the particles and a battery constructed with the cathode as well as methods for their formation are also provided.
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The invention claimed is: 1. A slurry, comprising: encapsulated chalcogen particles, comprising a chalcogen core and an encapsulate coating disposed on the chalcogen core surface consisting of at least one polymer having both hydrophobic regions and hydrophilic regions; carbon nanofibers; carbon black; carboxymethyl cellulose; styrene butadiene rubber; and water; wherein a sulfur content of the encapsulated chalcogen particles is greater than 90 wt % relative to the total dry weight of the encapsulated chalcogen particles, a content of sulfur is greater than 85 wt % relative to a total dry weight of the slurry; and a ratio of carbon nanofibers to carbon black is 3:1. 2. The slurry of claim 1 , wherein a total content of the carbon nanofiber and carbon black is less than 10 wt % relative to the total dry weight of the slurry. 3. The slurry of claim 1 , wherein a total content of the carboxymethyl cellulose and styrene butadiene rubber is less than 5 wt % relative to the total dry weight of the slurry. 4. The slurry of claim 1 , wherein a ratio of carboxymethyl cellulose to styrene butadiene rubber is 3:1. 5. The slurry of claim 1 , wherein water is present in an amount equal to 0.25-1.25 times the total dry weight of the slurry. 6. The slurry of claim 1 , wherein the chalcogen core further comprises at least one of selenium and tellurium. 7. The slurry of claim 1 , wherein the polymer coating consists of at least one polymer selected from the group consisting of poly (3,4-ethylenedioxythiophene) polystyrene sulfonate, polyvinylpyrrolidone, polyaniline, poly(ethylene oxide), carboxymethyl cellulose, sodium carboxymethyl cellulose, polymethacrylic acid, poly(2-acrylamido-2-methyl-1-propanesulfonic acid), branched polyethylenimine, and poly(diallyl dimethylammonium chloride). 8. The slurry of claim 6 , wherein a selenium content or a tellurium content of the encapsulated chalcogen particles is less than 50 wt % relative to a total weight of the encapsulated chalcogen particles. 9. The slurry of claim 6 , wherein the encapsulated chalcogen core further comprises carbon black particles, functionalized carbon black particles or both which are homogeneously dispersed in the chalcogen core. 10. A method for forming the slurry of claim 1 , comprising: forming a powder mixture comprising 90 wt % of the encapsulated chalcogen particles relative to the total dry weight of the slurry and 8 wt % of carbon nanofibers and carbon black together relative to the total dry weight of the slurry; grinding the powder mixture to form a powder of carbon and active material; adding a weight corresponding to 2 wt % of carboxymethyl cellulose and styrene butadiene rubber together relative to the total dry weight of the slurry to the powder of carbon and active material to form a thick slurry; adding water to the thick slurry; mixing the thick slurry to form the slurry. 11. The method of claim 10 , wherein water is added in an amount of 0.4-1.2 mL per g of the thick slurry. 12. The method of claim 10 , wherein the mixing is performed by planetary centrifugation for up to 15 minutes at a speed of greater than 1000 rpm. 13. The method of claim 10 , further comprising ball milling the fine powder of carbon and active material for up to 2 hours at a speed of less than 200 rpm. 14. An electrode, comprising: the dried slurry of claim 1 as active material; and a current collector; wherein the dried slurry is on a surface of the current collector. 15. The electrode of claim 14 , wherein a sulfur weight per current collector area is in the range of 3-8 mg/cm 2 . 16. The electrode of claim 14 , wherein the current collector comprises aluminum. 17. A method for forming the electrode of claim 14 , comprising: pouring the slurry onto the current collector forming a wet gap of less than 200 μm to obtain a green electrode; drying the green electrode; and calendering the dried green electrode to form the electrode. 18. The method of claim 17 , wherein the drying is performed in an oven at a temperature of up to 100° C. for up to 12 hours. 19. The method of claim 17 , wherein the dried green electrode is calendered such that the electrode has less than 50% of the thickness of the dried green electrode. 20. A battery, comprising: the electrode of claim 14 as a cathode; an anode; and an electrolyte in a solvent. 21. The battery of claim 20 , wherein the anode comprises a metal selected from the group consisting of an alkali metal and an alkaline earth metal. 22. The battery of claim 20 , wherein the anode is lithium and the electrolyte comprises LiTFSI and LiNO 3 in a molar ratio of 5:1. 23. The battery of claim 22 , wherein the solvent comprises glyme and dioxolane in a weight ratio of 1:1. 24. The battery of claim 20 , wherein the anode is lithium and the anode is pretreated with a lithium polysulfide. 25. A vehicle comprising the battery of claim 20 .
as layered products · CPC title
characterised by the solutes · CPC title
Rolling or calendering · CPC title
Chalcogenides or intercalation compounds thereof · CPC title
Carbon or graphite · CPC title
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