Chemical methods for treating a metathesis feedstock
US-9216941-B2 · Dec 22, 2015 · US
US2017321129A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017321129-A1 |
| Application number | US-201715660179-A |
| Country | US |
| Kind code | A1 |
| Filing date | Jul 26, 2017 |
| Priority date | Aug 26, 2015 |
| Publication date | Nov 9, 2017 |
| Grant date | — |
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The present disclosure provides a method, for removing sulfur compounds from a fuel containing sulfur compounds. The method includes contacting the fuel with an adsorbent that comprises a carbonaceous material doped with nanoparticles of aluminum oxide to reduce the concentrations of the sulfur compounds, the carbonaceous material is at least one selected from the group consisting of activated carbon, carbon nanotubes, and graphene oxide, and the adsorbent has a weight ratio of C to Al in the range from 3:1 to 30:1, and a weight ratio of C to O in the range from 1:1 to 10:1.
Opening claim text (preview).
1 . A method of reducing thiophene concentration in a diesel fuel, comprising: contacting the diesel fuel with a fixed bed adsorbent, wherein the fixed bed adsorbent comprises a carbonaceous material doped with nanoparticles of aluminum oxide, wherein the contacting forms a treated diesel fuel having a reduced concentration of thiophene, wherein the carbonaceous material is at least one selected from the group consisting of activated carbon, carbon nanotubes, and graphene oxide, and wherein the fixed bed adsorbent has a weight ratio of C to Al in the range from 3:1 to 30:1, and a weight ratio of C to O in the range from 3:1 to 9:1. 2 . The method of claim 1 , wherein the carbon nanotubes are multi-walled carbon nanotubes. 3 . The method of claim 1 , wherein the carbonaceous material is doped with the nanoparticles of aluminum oxide by incipient wetness impregnation. 4 - 6 . (canceled) 7 . The method of claim 1 , further comprising regenerating the adsorption ability of the fixed bed adsorbent. 8 . The method of claim 7 , wherein the regenerating comprises heating the fixed bed adsorbent at about 300-550° C. to remove the adsorbed sulfur compounds. 9 . The method of claim 1 , wherein the fixed bed adsorbent is disposed in a fixed bed or fluidized bed and the contacting involves passing the diesel fuel through the fixed bed or fluidized bed. 10 . The method of claim 9 , wherein the fixed bed comprises a cartridge. 11 . The method of claim 10 , wherein the cartridge further comprises at least one adsorbent selected from the group consisting of a zeolite, activated alumina, and activated carbon. 12 . (canceled) 13 . The method of claim 1 , wherein the carbon nanotubes have an outer diameter ranging from about 10 nm to 30 nm. 14 . The method of claim 1 , wherein the nanoparticles of aluminum oxide have a diameter ranging from about 30 nm to 80 nm. 15 - 19 . (canceled)
Recovery of used adsorbent · CPC title
Diesel oil · CPC title
Specific sorbent material, not covered by C10G25/02 or C10G25/03 · CPC title
Carbon nanostructures, e.g. nanotubes, nanohorns, nanocones, nanoballs (carbon nanotubes per se C01B32/15) · CPC title
Heteroatoms content, i.e. S, N, O, P · CPC title
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