Low temperature synthesis of aluminum hydr(oxide) inside porous media
US-10927016-B2 · Feb 23, 2021 · US
US11396004B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11396004-B2 |
| Application number | US-201916355016-A |
| Country | US |
| Kind code | B2 |
| Filing date | Mar 15, 2019 |
| Priority date | Mar 15, 2019 |
| Publication date | Jul 26, 2022 |
| Grant date | Jul 26, 2022 |
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A method for preparing a nano-enabled activated carbon block, a nano-enabled activated carbon block produced by the method, a household water filtration system comprising the nano-enabled activated carbon block, and a method for filtering tap water using the household water filtration system are provided. The method includes contacting a solution including a metal(lic) precursor (e.g. a titanium compound and/or an iron compound and/or a zirconium compound) with activated carbon particles such that the solution fills pores of the activated carbon particles. The method further includes causing a metal (hydr)oxide (e.g. titanium dioxide and/or zirconium dioxide and/or iron oxide) to precipitate from the solution thereby causing metal oxide nanoparticles to become deposited within pores of the activated carbon particles. The method also includes preparing a nano-enabled activated carbon block from the activated carbon particles having metal oxide nanoparticles deposited within the pores thereof.
Opening claim text (preview).
What is claimed is: 1. A method of preparing an activated carbon block, the activated carbon block comprising activated carbon defining pores and iron hydroxide (Fe(OH) 3 ) particles disposed in the pores, said method comprising: providing a solution comprising anhydrous iron trichloride (FeCl 3 ) and an alcohol; providing activated carbon particles; combining the solution and the activated carbon particles to form a slurry; raising pH of the slurry such that Fe(OH) 3 precipitates out of the solution producing activated carbon particles comprising the activated carbon particles with Fe(OH) 3 nanoparticles deposited within the pores thereof; rinsing the activated carbon particles with water to remove byproducts and/or impurities therefrom; rinsing the activated carbon particles with a neutralizing agent to neutralize the activated carbon particles; drying the activated carbon particles; and forming the activated carbon block with the activated carbon particles. 2. The method of claim 1 , wherein the step of forming the activated carbon block with the activated carbon particles comprises: combining the activated carbon particles with a binder to form a mass; compressing the mass at a pressure of from about 30 psi to about 120 psi; and heating the mass under pressure to a temperature of from about 175° C. to about 205° C. thereby producing the activated carbon block; and further comprising: cooling the activated carbon block; optionally, flushing the activated carbon block with water; optionally, wherein the activated carbon particles include a mean particle diameter in the range of about 60 to about 80 μm and a particle size distribution having less than 10 wt. % particles larger than 140 mesh and less than 10 wt. % particles smaller than 500 mesh, wherein wt. % is measured with respect to a total mass of the activated carbon; optionally, wherein the binder comprises an ultra-high molecular weight binder, optionally the ultra-high molecular weight binder having a melt index of not more than 1 g/min as measured using ASTM D1238 at 190° C. and 15 kg load. 3. The method of claim 1 , wherein: i) the activated carbon block comprises from about 20 wt. % to about 35 wt. % iron; ii) optionally, the alcohol comprises methanol. 4. The method of claim 3 , wherein ii) the alcohol comprises methanol. 5. The method of claim 1 , wherein: the activated carbon particles include a mean particle diameter in the range of about 60 to about 80 μm and a particle size distribution having less than 10 wt. % particles larger than 140 mesh and less than 10 wt. % particles smaller than 500 mesh, wherein wt. % is measured with respect to a total mass of the activated carbon; and the binder comprises an ultra-high molecular weight binder, optionally the ultra-high molecular weight binder having a melt index of not more than 1 g/min as measured using ASTM D1238 at 190° C. and 15 kg load. 6. The method of claim 1 , wherein pH of the slurry is raised to about 12 in the step of raising pH of the slurry. 7. A method of preparing an activated carbon block, the activated carbon block comprising activated carbon defining pores and iron hydroxide (Fe(OH) 3 ) particles disposed in the pores, said method comprising: providing an activated carbon block formed from activated carbon particles and a binder; providing a solution comprising anhydrous iron trichloride (FeCl 3 ) and an alcohol; contacting the activated carbon block and the solution to fill the pores with the solution; raising pH of the solution such that Fe(OH) 3 precipitates out to form an activated carbon block comprising the activated carbon with Fe(OH) 3 nanoparticles deposited within pores thereof; rinsing the activated carbon block with water to remove byproducts and/or impurities therefrom; rinsing the activated carbon block with a neutralizing agent to neutralize the activated carbon block; optionally, flushing the activated carbon block with water; optionally, wherein the activated carbon particles include a mean particle diameter in the range of about 60 to about 80 μm and a particle size distribution having less than 10 wt. % particles larger than 140 mesh and less than 10 wt. % particles smaller than 500 mesh, wherein wt. % is measured with respect to a total mass of the activated carbon; optionally, wherein the binder comprises an ultra-high molecular weight binder, optionally the ultra-high molecular weight binder having a melt index of not more than 1 g/min as measured using ASTM D1238 at 190° C. and 15 kg load. 8. The method of claim 7 , wherein: i) the activated carbon block comprises from about 20 wt. % to about 35 wt. % iron; ii) optionally, the alcohol comprises methanol. 9. The method of claim 8 , wherein ii) the alcohol comprises methanol. 10. The method of claim 7 , wherein: the activated carbon particles include a mean particle diameter in the range of about 60 to about 80 μm and a particle size distribution having less than 10 wt. % particles larger than 140 mesh and less than 10 wt. % particles smaller than 500 mesh, wherein wt. % is measured with respect to a total mass of the activated carbon; and the binder comprises an ultra-high molecular weight binder, optionally the ultra-high molecular weight binder having a melt index of not more than 1 g/min as measured using ASTM D1238 at 190° C. and 15 kg load. 11. The method of claim 7 , wherein pH of the slurry is raised to about 12 in the step of raising pH of the slurry.
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