Metal organic framework-derived carbon aerogel, preparation method thereof and application in lithium ion batteries
US-12183924-B2 · Dec 31, 2024 · US
US12172898B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12172898-B2 |
| Application number | US-202117595274-A |
| Country | US |
| Kind code | B2 |
| Filing date | Oct 12, 2021 |
| Priority date | Sep 29, 2021 |
| Publication date | Dec 24, 2024 |
| Grant date | Dec 24, 2024 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Provided is a method for preparing a hard carbon anode of a lithium/sodium ion battery by biochar, which includes the following steps: S1 biochar pretreatment, S2, preparing a precursor material and S3 pyrolysis carbonization, by a modification of the biochar, setting carbonization temperature and carbonization time, and controlling a cooling rate, so that the obtained biochar generates amorphous carbon after carbonization with low graphitization degree, few surface defects, larger charge-discharge specific capacity, and stable performance in the cycle charging and discharging process; at the same time, the process of the application is relatively simple, and a special complex process is reduced; the present method is suitable for a large-scale industrial production without special adjustment or control of a morphology; and the product performance is relatively good and thus has certain competitive advantages.
Opening claim text (preview).
The invention claimed is: 1. A method for preparing a hard carbon anode of a lithium/sodium ion battery with a biochar, wherein it comprises: S1, biochar pretreatment: adding a hydrochloric acid to a modified biochar for a pickling for 3 to 12 hours, and then rinsing with a deionized water to neutrality; S2, precursor material preparation: pouring the rinsed biochar into a ball mill jar, adding an absolute ethanol for a milling and crushing, filtering and drying after the ball milling is completed to obtain the precursor material; and S3, pyrolysis carbonization: placing the precursor material obtained above in a tubular furnace, carbonizing in an argon atmosphere with a carbonization temperature of 1200 to 1300° C., a carbonization time of 0.5 to 3 hours, and an aeration rate of 10 to 30 mL/min; performing a heat preservation for 1 to 3 hours after the carbonization is finished, cooling to 800 to 1100° C., and then inletting the argon for a natural cooling to 25 to 30° C. to obtain a hard carbon anode material. 2. The method according to of claim 1 , wherein the modified biochar is prepared by impregnating the biochar in a modified liquid at 20 to 40° C. for 0.2 to 2.5 hours, and then drying at 150 to 200° C. 3. The method according to claim 2 , wherein the modified liquid is N-N dimethylformamide and m-aminophenylurea hydrochloride solution in a volume ratio of 1 to 5:3. 4. The method according to claim 1 , wherein a concentration of the hydrochloric acid in S1 is 0.5 to 1.5 M. 5. The method according to claim 1 , wherein a mass-volume ratio of the biochar and the hydrochloric acid in Si is 1:0.077 to 0.13 g/mL. 6. The method according to claim 1 , wherein a mass-volume ratio of the biochar and the absolute ethanol in S2 is 0.6 to 1.3:3 to 5 g/mL. 7. The method according to claim 1 , wherein a revolving speed of the ball mill jar in S2 is 200 to 500 rpm, and a ball milling time is 3 to 12 hours. 8. The method according to claim 1 , wherein a temperature elevation program of the tubular furnace in S3 is 30° C. to 1000° C.: a temperature elevation rate is 4 to 6° C./min, and 1000 to 1300° C.: the temperature elevation rate is 3 to 5° C./min. 9. The method according to claim 1 , wherein a cooling rate of the tubular furnace in S3 is 3 to 5° C./min.
for inserting or intercalating light metals · CPC title
Accumulators not provided for in groups H01M10/05-H01M10/34 · CPC title
Rocking-chair batteries, i.e. batteries with lithium insertion or intercalation in both electrodes; Lithium-ion batteries · CPC title
Electric properties · CPC title
by IR- or Raman-data · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.