Hydrocarbon Fluids
US-2024010939-A1 · Jan 11, 2024 · US
US9447344B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9447344-B2 |
| Application number | US-201514796496-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 10, 2015 |
| Priority date | Sep 20, 2011 |
| Publication date | Sep 20, 2016 |
| Grant date | Sep 20, 2016 |
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The invention relates to a process to manufacture advanced cellulosic gasolines. Dilute organic acids derived from pyrolized biomass are converted to their corresponding alcohols in a stand-alone hydrodeoxygenation unit followed by membrane pervaporation step to remove water. The alcohol product is blended directly into a neat hydrocarbon fuel basestock to make unadditized gasoline.
Opening claim text (preview).
The invention claimed is: 1. A method for producing a renewable gasoline from cellulosic biomass comprising: a) separating a cellulosic feedstream in an ionic separator to generate a polyol stream comprising at least one of sugars and polyols and an organic stream comprising one or more organic acids and water; b) generating hydrocarbons comprising alkanes from the polyol stream in a hydrotreating reactor and converting at least a portion of the hydrocarbons to isomerized gasoline range hydrocarbons in an isomerization reactor c) generating alcohol from the organic stream, at least a portion of the hydrocarbons from the hydrotreating reactor and hydrogen in a hydrodeoxygenation reactor d) separating the alcohol, water, and hydrogen in a cold separator, and removing water using a membrane separator; and e) producing one or more product renewable gasoline streams comprising the alcohols, at least a portion of the hydrocarbons from the hydrotreating reactor and the isomerized gasoline range hydrocarbons. 2. The method of claim 1 , wherein said hydrodeoxygenation reactor comprises a catalyst selected from the group consisting of CuO, ZnO, Fe2O3, CuO/ZnO, CuO/Fe2O3, ZnO/Fe2O3, CuO/ZnO/Fe2O3, CuO/ZnO/Al2O3, CuO/Al2O3/SiO2, CuO/Fe2O3/Al2O3/SiO2, and combinations thereof. 3. The method of claim 1 , wherein said membrane separator comprises a membrane selected from the group consisting of hydrophilic, hydrophobic, organophillic, polydimethylsiloxane (PDMS), polyvinyl alcohol (PVA), polyimide, ceramic, zeolite, amorphous silica, hybrid membranes, and combinations thereof.
to change the structural skeleton of some of the hydrocarbon content without cracking the other hydrocarbons present, e.g. lowering pour point; Selective hydrocracking of normal paraffins (C10G32/00 takes precedence; improving or increasing the octane number or aromatic content of naphtha C10G35/00) · CPC title
in the presence of hydrogen, hydrogen donors or hydrogen generating compounds · CPC title
for gasoline engines · CPC title
Renewables or materials of biological origin · CPC title
using bio-feedstock · CPC title
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