Metal organic framework-derived carbon aerogel, preparation method thereof and application in lithium ion batteries
US-12183924-B2 · Dec 31, 2024 · US
US11855274B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11855274-B2 |
| Application number | US-202117522151-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 9, 2021 |
| Priority date | Sep 24, 2021 |
| Publication date | Dec 26, 2023 |
| Grant date | Dec 26, 2023 |
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Provided are hard carbon beads, their preparation method, and an energy storage device comprising the same. Microwave heating is used to synthesize cross-linked phenolic formaldehyde for reducing energy consumption and controlling the crosslinking density of cured phenolic formaldehyde. The problems caused by high temperature heating and hydrothermal process for curing resin can be solved by the instant disclosure, which can increase the economic values of electrode and energy storage device comprising the hard carbon beads.
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What is claimed is: 1. A method of preparing hard carbon beads comprising: step (a): dissolving phenol-formaldehyde resin, a cross-linking reagent and a protection reagent into a solvent to form a mixture and heating the mixture by microwave for cross-linking reaction to obtain a suspension containing phenol-formaldehyde beads, wherein the phenol-formaldehyde resin is set to be 100 parts by weight, the cross-linking reagent is greater than or equal to 5 parts by weight and less than or equal to 70 parts by weight, the protection reagent is greater than or equal to 1 part by weight and less than or equal to 10 parts by weight, a heating temperature of microwave is greater than or equal to 100° C. and less than or equal to 180° C., the cross-linking reagent is selected from the group consisting of: hexamethylenetetramine, formaldehyde acetal, furfural, furfural alcohol and trimethylol phosphine oxide, and the protection reagent is selected from the group consisting of: polyvinyl alcohol, methyl cellulose and polyoxyethylene polyoxypropylene; step (b): drying the suspension containing phenol-formaldehyde beads to obtain phenol-formaldehyde beads; and step (c): subjecting the phenol-formaldehyde beads for carbonization under inert gas to obtain the hard carbon beads, wherein a carbonization temperature is greater than or equal to 500° C. and less than or equal to 1500° C.; and the hard carbon beads have a maximum particle size and a minimum particle size, and a ratio of the maximum particle size to the minimum particle size is greater than or equal to 1.021 and less than or equal to 1.098. 2. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin is set to be 100 parts by weight in step (a), and the cross-linking reagent is greater than or equal to 5 parts by weight and less than or equal to 50 parts by weight. 3. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin is set to be 100 parts by weight in step (a), and the cross-linking reagent is greater than or equal to 5 parts by weight and less than or equal to 30 parts by weight. 4. The method as claimed in claim 1 , wherein the carbonization temperature in step (c) is greater than or equal to 600° C. and less than or equal to 1500° C. 5. The method as claimed in claim 1 , wherein the carbonization temperature in step (c) is greater than or equal to 700° C. and less than or equal to 1200° C. 6. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin has a number average molecular weight greater than or equal to 200 and less than or equal to 10000. 7. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin is nitrogen-doped phenol-formaldehyde resin or phenol-formaldehyde resin without nitrogen doping. 8. The method as claimed in claim 1 , wherein the solvent comprises 0 vol % to 100 vol % water and 0 vol % to 100 vol % alcohol, and the alcohol is methanol, ethanol or the combination thereof. 9. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin has a number average molecular weight greater than or equal to 200 and less than or equal to 3000 and the solvent is water, methanol or ethanol. 10. The method as claimed in claim 1 , wherein the phenol-formaldehyde resin has a number average molecular weight greater than or equal to 2000 and less than or equal to 4000 and the solvent comprises 20 vol % to 80 vol % water and 20 vol % to 80 vol % methanol or ethanol. 11. A hard carbon bead having a maximum particle size and a minimum particle size, wherein a ratio of the maximum particle size to the minimum particle size is greater than or equal to 1.021 and less than or equal to 1.098. 12. The hard carbon bead as claimed in claim 11 , wherein the hard carbon bead has an average group particle size greater than or equal to 3.5 μm and less than or equal to 4.8 μm. 13. The hard carbon bead as claimed in claim 11 , wherein the hard carbon bead has an average group particle size greater than or equal to 3.8 μm and less than or equal to 4.6 μm. 14. The hard carbon bead as claimed in claim 12 , wherein the hard carbon bead has a standard deviation of particle size greater than or equal to 1.2 μm and less than or equal to 2.8 μm. 15. The hard carbon bead as claimed in claim 11 , wherein the hard carbon bead has a graphitic length L a micro structure greater than or equal to 2.9 nm and less than or equal to 3.5 nm. 16. The hard carbon bead as claimed in claim 11 , wherein the hard carbon bead has a graphitic length L a micro structure greater than or equal to 3.0 nm and less than or equal to 3.4 nm. 17. The hard carbon bead as claimed in claim 11 , wherein the Raman spectrum of the hard carbon bead has D1 band and G band, and the ratio of the intensity of D1 band to the intensity of G band is greater than or equal to 2.0 and less than or equal to 2.5. 18. An energy storage device comprising a negative electrode and a lithium foil as a counter electrode, wherein the negative electrode comprises the hard carbon beads as claimed in claim 11 , the negative electrode coupling with the counter electrode of lithium foil has a Galvanostatic charge-discharge curve, and the Galvanostatic charge-discharge curve comprises a plateau region ranging from 0.003 V to 0.12 V and a sloping area ranging from 0.12 V to 1.5 V, a specific capacity of the plateau region is greater than or equal to 90 mAh/g and less than or equal to 220 mAh/g, and a specific capacity of the sloping area is greater than or equal to 120 mAh/g and less than or equal to 320 mAh/g. 19. The energy storage device as claimed in claim 18 , wherein the energy storage device has a total specific capacity greater than or equal to 280 mAh/g and less than or equal to 500 mAh/g.
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