Carbon catalyst, method of producing same, and electrode and battery each utilizing same
US-9040452-B2 · May 26, 2015 · US
US10328381B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10328381-B2 |
| Application number | US-201615246943-A |
| Country | US |
| Kind code | B2 |
| Filing date | Aug 25, 2016 |
| Priority date | Feb 25, 2016 |
| Publication date | Jun 25, 2019 |
| Grant date | Jun 25, 2019 |
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Disclosed is an activated carbon including pores formed on a surface thereof, in particular, the pores include ultra-micropores having a diameter that is equal to or less than about 1.0 nm.
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What is claimed is: 1. A method of manufacturing an activated carbon, the method comprising: preparing a carbon precursor; carbonizing the carbon precursor by heat treating thereon; equalizing the carbon precursor carbonized by grinding them; and activating the equalized carbon precursor by adding an oxidizing agent and distilled water into the equalized carbon precursor and heat treating thereon, to form the activated carbon, wherein a volume of the oxidizing agent is in a range of about 10 volume % to 50 volume % for a total of 100 volume % of the oxidizing agent and the distilled water, in the activating, wherein the oxidizing agent includes H 2 O 2 , and wherein the activating is performed at a temperature in a range of about 700° C. to 1000° C. 2. The method of claim 1 , wherein the activating is performed while injecting a mixture of the oxidizing agent and the distilled water into the carbon precursor at a speed of about 1 ml/h to 100 ml/h. 3. The method of claim 2 , wherein the activating is performed under a pressure that is in a range of 0 bar to about 5 bar. 4. The method of claim 1 , wherein the activating is performed for a time that is in a range of about 1 h to 5 h. 5. The method of claim 1 , further comprising reducing a surface of the activated carbon by heat treating thereon under an atmosphere including hydrogen (H 2 ). 6. The method of claim 5 , wherein the reducing is performed under a mixing environment in which an inert gas and hydrogen (H 2 ) gas are mixed, and a volume of the hydrogen (H 2 ) gas is in a range of greater than 0 volume % to about 10 volume % for a total of 100 volume % of the inert gas and hydrogen (H 2 ) gas. 7. The method of claim 5 , wherein the reducing is performed at a temperature in a range of about 700° C. to 1000° C. 8. The method of claim 5 , wherein the reducing is performed for about 5 h to 10 h. 9. The method of claim 1 , further comprising selecting the equalized carbon precursor by using a sieve having a size in a range of about 100 um to 250 um, after the equalizing. 10. The method of claim 1 , wherein the equalizing is performed by using a ball mill, and a particle size of a ball used for the ball mill is in a range of about 1 mm to 20 mm. 11. The method of claim 10 , wherein a volume of the carbon precursor is in a range of about 0.1 volume % to 40 volume % for a total of 100 volume % of the carbon precursor and the ball mill, in the equalizing. 12. The method of claim 10 , wherein a processing speed for the ball mill is in a range of about 100 rpm to 500 rpm, in the equalizing. 13. The method of claim 10 , wherein a processing time for the ball mill is in a range of 30 minutes to 5 hours, in the equalizing. 14. The method of claim 1 , wherein the carbonizing is performed at a temperature that is in a range of about 700° C. to 1000° C. 15. The method of claim 1 , wherein the carbon precursor includes starch, coconut husks, citrus peel, coffee grounds, bamboo stems, or a combination thereof.
characterised by non-gaseous activating agents · CPC title
Addition of pore forming agents, e.g. pore inducing or porogenic agents · CPC title
Surface area, e.g. BET-specific surface · CPC title
being more than 50 nm, i.e. macropores · CPC title
of nitrous oxide (N2O) · CPC title
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