US2022306478A1PendingUtilityA1
Silicon material and method of manufacture
Est. expiryNov 13, 2040(~14.3 yrs left)· nominal 20-yr term from priority
C01P 2004/32C01B 33/023C01P 2004/84C01B 32/20C01P 2006/90B82Y 30/00H01M 4/366Y02E60/10C01P 2006/16H01M 4/386B82Y 40/00C01P 2004/64C01P 2006/12H01M 4/625H01M 2004/021C01P 2004/90Y02P70/50H01M 4/583H01M 2004/027C01B 33/02
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Abstract
A method for manufacturing a silicon material can include comminuting a silicon material. A silicon material can include silicon nanoparticles formed by comminuting silicon particles, where the silicon nanoparticles can cooperatively form pores.
Claims
exact text as granted — not AI-modifiedWe claim:
1 . A silicon material comprising:
silicon nanoparticles with a mean size between about 50-200 nm, wherein the silicon nanoparticles are spheroidal, wherein the silicon nanoparticles comprise 3-37% oxygen by mass, wherein the silicon nanoparticles are formed by comminuting silicon particles comprising at least 99% silicon by mass.
2 . The silicon material of claim 1 , wherein a surface of a silicon nanoparticle is fused to a surface of adjacent silicon nanoparticles.
3 . The silicon material of claim 2 , wherein the silicon nanoparticles cooperatively define a void space between adjacent silicon nanoparticles.
4 . The silicon material of claim 3 , wherein a characteristic dimension of the void space is between 0.5 and 500 nm.
5 . The silicon material of claim 1 , wherein the silicon nanoparticles are nonporous.
6 . The silicon material of claim 1 , further comprising a graphitic coating disposed on the silicon nanoparticles with a thickness between 1-10 nm.
7 . The silicon material of claim 1 , wherein the silicon nanoparticles comprise a 1-5 nm thick surface layer of silicon oxide.
8 . The silicon material of claim 1 , further comprising a polymer coating disposed on the silicon nanoparticles.
9 . The silicon material of claim 8 , wherein the polymer coating comprises at least one of: polytetrafluoroethylene, polyvinylidene fluoride, polyacrylic acid, carboxymethyl cellulose, styrene-butadiene rubber, polyacrylonitrile, alginate, polyimide, polyamide, polyaniline, polypyrrole, poly(thiophene), or poly(3,4-ethylenedioxythiophene).
10 . The silicon material of claim 1 , wherein a size distribution of the silicon nanoparticles is a mollified uniform distribution.
11 . A method for manufacturing a silicon material comprising:
reducing a silica precursor to produce silicon particles comprising at least 99% silicon by mass, wherein a mean characteristic size of the silicon particles is between about 2 μm and 50 μm; and comminuting the silicon particles to prepare comminuted silicon particles with a mean characteristic size between about 50-200 nm.
12 . The method of claim 11 , wherein the silicon particles are spheroidal.
13 . The method of claim 12 , wherein the comminuted silicon particles are spheroidal.
14 . The method of claim 11 , wherein comminuting the silicon particles comprises continuously ball milling the silicon particles for between 1 and 12 hours.
15 . The method of claim 14 , wherein the silicon particles are ball milled at a speed between 100 and 600 rpm.
16 . The method of claim 11 , further comprising oxidizing the comminuted silicon particles, wherein the comminuted silicon particles comprise 3-37% oxygen by mass.
17 . The method of claim 16 , wherein oxidizing the comminuted silicon comprises heating the comminuted silicon particles in an oxidizing environment to a temperature between 200-1000° C. for 1-24 hours.
18 . The method of claim 11 , further comprising coating the comminuted silicon particles with a carbonaceous material.
19 . The method of claim 18 , wherein coating the comminuted silicon particles comprises growing the carbonaceous material on the comminuted silicon particles using chemical vapor deposition.
20 . The method of claim 19 , wherein growing the carbon carbonaceous material comprises:
heating the comminuted silicon particles to a temperature between 700-950° C. under an inert gas flow rate between 50 and 500 sccm and a hydrogen gas flow rate between 20 and 100 sccm; further heating the comminuted silicon particles to a temperature between 900 and 1100° C. and introducing at least one of methane or ethyne at a flow rate between 20 and 200 sccm, where the at least one of methane or ethyne is introduced for between 5 minutes and 2 hours.Cited by (0)
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