Liquid Electrolyte Composition, and Electrochemical Cell Comprising Said Electrolyte Composition
US-2024347772-A1 · Oct 17, 2024 · US
US2025062319A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2025062319-A1 |
| Application number | US-202318449261-A |
| Country | US |
| Kind code | A1 |
| Filing date | Aug 14, 2023 |
| Priority date | Aug 14, 2023 |
| Publication date | Feb 20, 2025 |
| Grant date | — |
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A method is provided for pre-forming anode particles for use in lithium ion batteries. The pre-formed anode particles bear a solid electrolyte of a composition that cannot be formed in situ in the battery. The method includes providing a dispersion of anode precursor particles and an additive not found in the battery in a liquid electrolyte solution. Applying a voltage or current across the dispersion forms the solid electrolyte interphase, on the particles. These particles can be used in an electrode of a lithium ion battery.
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What is claimed is: 1 . A method of pre-forming anode particles bearing a solid electrolyte interphase, the anode particles being for use in an anode of a lithium ion battery, where the lithium ion battery includes the anode, an anode current collector, a cathode, a cathode current collector, an optional separator, and a battery electrolyte, the method comprising: providing a dispersion in a vessel configured for electrochemical reactions, wherein the dispersion comprises anode precursor particles and a first liquid electrolyte solution, and the dispersion includes an additive not found in the lithium ion battery, applying a voltage across the dispersion or applying a current across the dispersion to form the anode particles bearing the solid electrolyte interphase, and recovering the anode particles bearing the solid electrolyte interphase from the dispersion. 2 . The method of claim 1 wherein the additive is present in the dispersion before applying the voltage or the current. 3 . The method of claim 1 wherein the additive is added to the dispersion during the application of the voltage or the current. 4 . The method of claim 2 wherein after applying the voltage or the current and during the application of the voltage or the current, introducing an additional additive to the dispersion to form a solid electrolyte interphase having a first layer of a first composition and a second layer of a second composition. 5 . The method of claim 4 further comprising repeating the step of introducing an additional additive and applying the voltage after introducing the additional additive. 6 . The method of claim 1 wherein the anode particles comprise silicon, germanium, tin, bismuth, graphite, antimony, silicon oxide, or a combination of two or more thereof. 7 . The method of claim 1 wherein the anode particles have an average particle size of from 50 nanometers to 100 micrometers. 8 . The method of claim 1 wherein the solid electrolyte interphase has a thickness of 1 to 100 nanometers. 9 . The method of claim 1 wherein the first liquid electrolyte solution comprises a salt in a solvent wherein the salt comprises lithium bis(fluorosulfonyl)imide, lithium bis(trifluoromethanesulfonyl)imide, lithium bis(oxalato) borate, lithium difluorooxalatoborate, or 1,1,2,2-tetra-fluoroethyl-2,2,3,3-tetrafluoropropyl ether and/or the solvent comprises ethylene carbonate, dimethyl carbonate, ethyl methyl carbonate, diethyl carbonate, propylene carbonate, dimethyl sulfoxide, ethyl acetate, gamma butyrolactone, 1,2-dimethoxyethane, or tetraethylene glycol dimethyl ether. 10 . The method of claim 1 wherein the additive comprises a fluorinated carbonate, a vinylene carbonate, an alkoxy silane, or an alkyl acrylamide. 11 . The method of claim 1 wherein the dispersion comprises 1 to 25 weight percent of the anode particles, and 0.001 to 10 weight percent of the additive based on total weight of the dispersion. 12 . The method of claim 1 wherein the electrochemical reaction vessel comprises a conductive shell as a current collector and an electrode comprising lithium metal. 13 . The method of claim 1 wherein voltage is applied at a level of +/−10 to +/−7000 millivolts. 14 . The method of claim 1 wherein current is applied at a level of from +/−0.01 to +/−10 milliamps per square centimeter. 15 . The method of claim 1 wherein the solid electrolyte interphase is a homogeneous composition. 16 . The method of claim 1 wherein the solid electrolyte interphase has a composition which varies along a gradient from a surface of the anode particle to a surface of the solid electrolyte interphase. 17 . The method of claim 1 wherein the solid electrolyte interphase is inorganic, organic, or a combination thereof. 18 . The method of claim 1 further comprising forming a second dispersion comprising the anode particles bearing the solid electrolyte interphase, and a second liquid electrolyte solution which is different from first liquid electrolyte solution and applying a voltage or a current across the dispersion to form a second layer of solid electrolyte interphase on the anode particles. 19 . The method of claim 1 comprising forming a slurry comprising the anode particles bearing the solid electrolyte interphase, a binder, a conductive component and solvent, applying the slurry to a current collector, drying and optionally curing to form an anode. 20 . A lithium ion battery comprising an anode disposed on an anode current collector, a cathode disposed on a cathode current collector, an optional separator, disposed between the anode and the cathode, and a battery electrolyte, wherein the anode comprises anode particles having a pre-formed solid electrolyte interphase of a composition that could not be formed in situ in the lithium ion battery.
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