Metal organic framework-derived carbon aerogel, preparation method thereof and application in lithium ion batteries
US-12183924-B2 · Dec 31, 2024 · US
US2021184216A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2021184216-A1 |
| Application number | US-201816761662-A |
| Country | US |
| Kind code | A1 |
| Filing date | Nov 6, 2018 |
| Priority date | Nov 6, 2017 |
| Publication date | Jun 17, 2021 |
| Grant date | — |
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A negative electrode active material including a silicon-carbon-based particle, the silicon-carbon-based particle having a SiCx matrix and boron doped in the SiCx matrix, wherein x of the SiCx matrix is 0.3 or more and less than 0.6.
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1 . A negative electrode active material, comprising: a silicon-carbon-based particle, wherein the silicon-carbon-based particle comprises: a SiC x matrix; and boron doped in the SiC x matrix, wherein x of the SiC x matrix is 0.3 or more and less than 0.6. 2 . The negative electrode active material of claim 1 , wherein the boron is present in an amount of 0.5 wt % to 1 wt % based on a total weight of the silicon-carbon-based particle. 3 . The negative electrode active material of claim 1 , wherein an average particle diameter (D 50 ) of the silicon-carbon-based particles is 1 μm to 10 μm. 4 . The negative electrode active material of claim 1 , wherein the SiC x matrix comprises SiC and Si. 5 . The negative electrode active material of claim 1 , wherein the boron is present inside the SiC x matrix. 6 . A method for preparing a negative electrode active material, the method comprising: forming a matrix fluid by performing a first heat treatment wherein vaporized silicon source, carbon source, and carrier gas are introduced into a first reaction furnace; and reacting the matrix fluid and boron in the gaseous state to form a SiC matrix doped with boron, wherein x of the SiC x matrix is 0.3 or more and less than 0.6. 7 . The method of claim 6 , wherein in the step of forming of the matrix fluid, a ratio of an inflow rate of the vaporized silicon source to an inflow rate of the carbon source is 1:0.3 to 1:0.6. 8 . The method of claim 6 , wherein the first heat treatment is performed at a temperature range of 1500° C. to 2500° C. 9 . The method of claim 6 , wherein the carrier gas is at least one selected from the group consisting of Ar, He, and Ne. 10 . The method of claim 6 , wherein the step of forming of a SiC x matrix doped with boron comprises performing a second heat treatment by introducing the matrix fluid and the boron in the gaseous state into a second reaction furnace. 11 . The method of claim 10 , wherein a temperature of the second heat treatment is in a range of 2000° C. to 2800° C. 12 . The method of claim 10 , wherein a ratio of an inflow rate of the matrix fluid to an inflow rate of the boron in the gaseous state is 300:1 to 600:1. 13 . A negative electrode comprising the negative electrode active material of claim 1 . 14 . The negative electrode of claim 13 further comprising, a graphite-based active material. 15 . A secondary battery comprising: the negative electrode of claim 13 ; a positive electrode: a separator interposed between the positive electrode and the negative electrode; and an electrolyte.
Carbon or graphite · CPC title
one element only · CPC title
Electric properties · CPC title
Silicon or alloys based on silicon · CPC title
for inserting or intercalating light metals · CPC title
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