Abstract: A gasoline fuel formulation which contains 60% v/v or more of a combination of (a) a biologically-derived alcohol and (b) a mixture of C4 to C12 hydrocarbon fuel components, all of which hydrocarbon fuel components have been derived, whether directly or indirectly, from catalytic conversion of a biologically-derived oxygenate component, wherein the concentration of the alcohol (a) in the formulation is from 0.1 to 30% v/v.

Abstract: A gasoline fuel formulation which contains 60% v/v or more of a combination of (a) a biologically-derived alcohol and (b) a mixture of C4 to C12 hydrocarbon fuel components, all of which hydrocarbon fuel components have been derived, whether directly or indirectly, from catalytic conversion of a biologically-derived oxygenate component, wherein the concentration of the alcohol (a) in the formulation is from 0.1 to 30% v/v.

Abstract: Reduced emissions in a jet fuel having aromatics content can be achieved by incorporating a quantity of an aromatic kerosene fuel blending component, preferably a bio-derived synthetic aromatic kerosene, comprising at least 90 wt. % of aromatics, less than 10 wt. % of indanes and tetralins and less than 1 wt. % of naphthalene into a jet fuel in a manner to meet the aromatic content specification for jet fuels. A jet fuel having aromatics content having reduced number-based nvPM emissions compared to equivalent total aromatics content petroleum-derived kerosene jet fuel is obtained.

Abstract: A moderate fraction of a carbohydrate derived component, and a kerosene composition comprising the moderate fraction.

Abstract: A moderate fraction of a carbohydrate derived component, and a kerosene composition comprising the moderate fraction, the moderate fraction having at least one C4+ compound, wherein: the moderate fraction exhibits: a mean percentage of 99% or more biobased material, as determined by C14 testing; and, a final boiling point in the range of from 200 to 320° C.; and, the moderate fraction comprises: a first quantity of one or more branched carbohydrate derived C4+ alkanes; a second quantity of one or more straight chain carbohydrate derived C4+ alkanes; a concentration of one or more substituted carbohydrate derived C5+ cycloalkanes comprising substituents selected from the group consisting of branched C3-4 alkyls and straight chain C1-4 alkyls, at least some of the substituted carbohydrate derived C5+ cycloalkanes comprising fused cycloalkanes.

Abstract: Liquid fuel compositions comprising one or more C4+ compounds derived from a water soluble oxygenated hydrocarbon.

Abstract: The application provides a moderate fraction of a carbohydrate derived component having at least one C4+ compound (and kerosene fuel composition comprising same), the moderate fraction exhibiting a mean percentage of 99% or more biobased material, as determined by C14 testing, the moderate fraction comprising: one or more substituted carbohydrate derived cycloalkanes comprising one or more substituent selected from the group consisting of branched C3-4 alkyls, straight chain C1-4 alkyls, branched C3-4 alkylenes, and straight chain C1-4 alkylenes; one or more carbohydrate derived aromatics, at least some of the carbohydrate derived aromatics comprising one or more substituent selected from the group consisting of branched C3-4 alkyls, straight chain C1-4 alkyls, branched C3-4 alkylenes, and, straight chain C2-4 alkylenes; and one or more carbohydrate derived compound selected from the group consisting of fused aryls, indane, indene, isomers thereof, and combinations thereof, at least some of the carbohydrate d

Abstract: The present invention provides a liquid fuel composition comprising a distillation fraction of a component having at least one C4+ compound derived from a water-soluble oxygenated hydrocarbon prepared by a method comprising: providing water and a water-soluble oxygenated hydrocarbon comprising a C1+O1+ hydrocarbon in an aqueous liquid phase and/or a vapor phase; providing H2; catalytically reacting in the liquid and/or vapor phase the oxygenated hydrocarbon with the H2 in the presence of a deoxygenation catalyst at a deoxygenation temperature and deoxygenation pressure to produce an oxygenate comprising a C1+O1-3 hydrocarbon in a reaction stream; and catalytically reacting in the liquid and/or vapor phase the oxygenate in the presence of a condensation catalyst at a condensation temperature and condensation pressure to produce the C4+ compound, wherein the C4+ compound comprises a member selected from the group consisting of C4+ alcohol, C4+ ketone, C4+ alkane, C4+ alkene, C5+ cycloalkane, C5+ cycloalkene,

Abstract: Liquid fuel compositions comprising one or more C4+ compounds derived from a water-soluble oxygenated hydrocarbon.

Abstract: Processes and reactor systems are provided for the conversion of sugars to sugar alcohols using a hydrogenation catalyst, which includes apparatus and method for in-line regeneration of the hydrogenation catalyst to remove carbonaceous deposits.

Abstract: Liquid fuel compositions comprising one or more C4+ compounds derived from a water-soluble oxygenated hydrocarbon.

Abstract: The present invention provides a liquid fuel composition comprising a distillation fraction of a component having at least one C4+ compound derived from a water-soluble oxygenated hydrocarbon prepared by a method comprising: providing water and a water-soluble oxygenated hydrocarbon comprising a C1+O1+ hydrocarbon in an aqueous liquid phase and/or a vapor phase; providing H2; catalytically reacting in the liquid and/or vapor phase the oxygenated hydrocarbon with the H2 in the presence of a deoxygenation catalyst at a deoxygenation temperature and deoxygenation pressure to produce an oxygenate comprising a C1+O1-3 hydrocarbon in a reaction stream; and catalytically reacting in the liquid and/or vapor phase the oxygenate in the presence of a condensation catalyst at a condensation temperature and condensation pressure to produce the C4+ compound, wherein the C4+ compound comprises a member selected from the group consisting of C4+ alcohol, C4+ ketone, C4+ alkane, C4+ alkene, C5+ cycloalkane, C5+ cycloalkene,

Abstract: A process for saturating benzene in a light paraffin isomerization process can accommodate varying quantities of benzene through the incorporation of progressive steps that control temperatures in the isomerization zone while performing a majority of the saturation within an immediately upstream benzene saturation zone. The process is suited for saturating benzene to very low levels while feedstream concentrations of benzenes may vary from 2 to 25 wt % throughout a given period of operation. The process can accommodate rapid swings in benzene concentration that may occur on a daily basis. The invention is particularly suited for the use of a sulfated zirconia catalyst that allows the utilization of existing reactor vessels in an isomerization process.

Abstract: A process for saturating benzene in a light paraffin isomerization process can accommodate varying quantities of benzene through the incorporation of progressive steps that control temperatures in the isomerization zone while performing a majority of the saturation within an immediately upstream benzene saturation zone. The process is suited for saturating benzene to very low levels while feedstream concentrations of benzenes may vary from 2 to 25 wt % throughout a given period of operation. The process can accommodate rapid swings in benzene concentration that may occur on a daily basis. The invention is particularly suited for the use of a sulfated zirconia catalyst that allows the utilization of existing reactor vessels in an isomerization process.