Porous oil binder and method for the production thereof
US-10519354-B2 · Dec 31, 2019 · US
US11517876B1 · US · B1
| Field | Value |
|---|---|
| Publication number | US-11517876-B1 |
| Application number | US-202217742089-A |
| Country | US |
| Kind code | B1 |
| Filing date | May 11, 2022 |
| Priority date | Dec 21, 2021 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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A method of forming an activated carbon sorbent from a seagrass. The method involves treating a seagrass with a base solution to form an intermediate solid, drying the intermediate solid to form a precursor, and pyrolyzing the precursor at 600 to 1000° C. to form the activated carbon sorbent. Preferably the seagrass is Halodule uninervis. The activated carbon sorbent is used in a method of removing an organic pollutant from a contaminated water. Preferred organic pollutants removed are phenols, specifically 2,4-dimethylphenol and 2,4-dichlorophenol.
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The invention claimed is: 1. A method of forming an activated carbon sorbent, the method comprising: treating a seagrass with a base solution to form an intermediate solid; drying the intermediate solid to form a precursor; and pyrolyzing the precursor at 600 to 1000° C. to form the activated carbon sorbent, wherein the activated carbon sorbent has a mean surface area of 1000 to 1250 m 2 /g, and wherein the activated carbon sorbent comprises, 70 to 92.5 wt % carbon; 15 to 23 wt % oxygen; 1 to 5 wt % calcium; 1 to 5 wt % magnesium; and 0.1 to 0.9 wt % potassium, each based on a total weight of activated carbon sorbent. 2. The method of claim 1 , wherein the seagrass is a member of the family Cymodoceaceae. 3. The method of claim 1 , wherein the seagrass is a member of the genus Halodule. 4. The method of claim 1 , wherein the seagrass is Halodule uninervis. 5. The method of claim 1 , wherein the pyrolyzing is performed under an inert atmosphere for 1 to 12 hours. 6. The method of claim 1 , wherein the base solution is an aqueous solution of a hydroxide base. 7. The method of claim 6 , wherein the base solution is used in an amount of 5 to 20 mmol hydroxide base per gram of seagrass. 8. The method of claim 1 , wherein the activated carbon sorbent has a mean pore volume of 0.400 to 0.525 cc g −1 . 9. The method of claim 1 , wherein the activated carbon sorbent has a point of zero charge pH (pH zpc ) of 8 to 11.5. 10. The method of claim 1 , wherein the activated carbon sorbent comprises 16 to 21 wt % oxygen based on a total weight of activated carbon sorbent. 11. The method of claim 1 , wherein the activated carbon sorbent comprises 17 to 19 wt % oxygen based on a total weight of activated carbon sorbent. 12. The method of claim 1 , wherein the activated carbon sorbent comprises 17.5 to 18 wt % oxygen based on a total weight of activated carbon sorbent. 13. The method of claim 1 , wherein the activated carbon sorbent consists of: 81.5 to 92.5 wt % carbon; 15 to 23 wt % oxygen; 1 to 5 wt % calcium; 1 to 5 wt % magnesium; and 0.5 to 0.9 wt % potassium, each based on a total weight of activated carbon sorbent.
in the liquid phase · CPC title
Regeneration or reactivation by electric current, ultrasound or irradiation, e.g. electromagnetic radiation such as X-rays, UV, light, microwaves · CPC title
of sorbents or filter aids comprising free carbon, e.g. activated carbon · CPC title
Thermal treatment, e.g. calcining or pyrolizing · CPC title
being in the range 0.5-1.0 ml/g · CPC title
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