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    • 21. 发明专利
    • Liquid fuel compositions based on catalytically deoxygenated and condensated oxygenated carbohydrates
    • AU2014202232B2
    • 2015-03-26
    • AU2014202232
    • 2014-04-23
    • SHELL INT RESEARCHVIRENT ENERGY SYSTEMS INC
    • BAULDREAY JOANNA MARGARETBLOMMEL PAUL GEORGECORTRIGHT RANDY DOUGLASPRICE RICHARD JOHN
    • C10G3/00C10L1/04
    • 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+Oi+ hydrocarbon in an aqueous liquid phase and/or a vapour phase; providing H2; catalytically reacting in the liquid and/or vapour 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 CI+01-3 hydrocarbon in a reaction stream; and catalytically reacting in the liquid and/or vapour 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, Cs+ cycloalkane, Cs+ cycloalkene, aryl, fused aryl, and a mixture thereof; wherein the liquid fuel composition is selected from: a gasoline composition having an initial boiling point in the range of from 15 'C to 70 'C (IP123), a final boiling point of at most 230 'C (IP123), a RON in the range of from 85 to 110 (ASTM 02699) and a MON in the range of from 75 to 100 (ASTM D2700); a diesel fuel composition having an initial boiling point in the range of from 130 'C to 230 'C (IP123), a final boiling point of at most 410 'C (IP123) and a cetane number in the range of from 35 to 120 (ASTM D613); and a kerosene composition having an initial boiling point in the range of from 80 to 150 'C, a final boiling point in the range of from 200 to 320 'C and a viscosity at -20 'C in the range of from 0.8 to 10 mm2/s (ASTM D445); and wherein the component having at least one C4+ compound derived from a water-soluble oxygenated hydrocarbon is less than 100 years old, as calculated from the carbon 14 concentration of the component. WO 2010/028206 PCT/U S2009/055976 Hydrogenolysis APR Acd y rc a on Biomass[- -~ grFAi- Hdoabn Hydrogenation De~x - aeand MonoOxygenates Condensation
    • 23. 发明专利
    • Liquid fuel compositions based on catalytically deoxygenated and condensated oxygenated carbohydrates
    • AU2014202232A1
    • 2014-05-29
    • AU2014202232
    • 2014-04-23
    • SHELL INT RESEARCHVIRENT ENERGY SYSTEMS INC
    • BAULDREAY JOANNA MARGARETBLOMMEL PAUL GEORGECORTRIGHT RANDY DOUGLASPRICE RICHARD JOHN
    • C10G3/00C10L1/04
    • 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+Oi+ hydrocarbon in an aqueous liquid phase and/or a vapour phase; providing H2; catalytically reacting in the liquid and/or vapour 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 CI+01-3 hydrocarbon in a reaction stream; and catalytically reacting in the liquid and/or vapour 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, Cs+ cycloalkane, Cs+ cycloalkene, aryl, fused aryl, and a mixture thereof; wherein the liquid fuel composition is selected from: a gasoline composition having an initial boiling point in the range of from 15 'C to 70 'C (IP123), a final boiling point of at most 230 'C (IP123), a RON in the range of from 85 to 110 (ASTM 02699) and a MON in the range of from 75 to 100 (ASTM D2700); a diesel fuel composition having an initial boiling point in the range of from 130 'C to 230 'C (IP123), a final boiling point of at most 410 'C (IP123) and a cetane number in the range of from 35 to 120 (ASTM D613); and a kerosene composition having an initial boiling point in the range of from 80 to 150 'C, a final boiling point in the range of from 200 to 320 'C and a viscosity at -20 'C in the range of from 0.8 to 10 mm2/s (ASTM D445); and wherein the component having at least one C4+ compound derived from a water-soluble oxygenated hydrocarbon is less than 100 years old, as calculated from the carbon 14 concentration of the component. WO 2010/028206 PCT/U S2009/055976 Hydrogenolysis APR Acd y rc a on Biomass[- -~ grFAi- Hdoabn Hydrogenation De~x - aeand MonoOxygenates Condensation
    • 29. 发明专利
    • USO DE UNA COMPOSICION DE COMBUSTIBLE
    • AR054436A1
    • 2007-06-27
    • ARP060101426
    • 2006-04-11
    • SHELL INT RESEARCH
    • CLAYTON CHRISTOPHER WILLIAMDAHLSTROM MARY ANNPRICE RICHARD JOHNSMITH SUSAN JANETAIT NIGEL PETERWALLINGTON JESSICA FLEE GEORGE ROBERTO
    • C10L1/08C10L10/04
    • El uso de una composicion de combustible que incluye la principal concentracion de combustible adecuada para ser utilizada en un motor de encendido por compresion, el combustible incluye uno o más hidrocarburos que entran en ebullicion dentro del rango de ebullicion de los combustible diesel, al menos uno de estos componentes hidrocarburo fueron tratados con un material adsorbente o un metal adsorbente en una fase física diferente a la del componente hidrocarburo, preferiblemente para reducir el nivel de al menos un metal, más preferiblemente el nivel de al menos un metal más pasado, más preferentemente el nivel de zinc, en dicho componente hidrocarburo, para reducir la emision de NOx, y opcionalmente partículas, del motor de encendido por compresion hacia las cámaras de combustion de las cuales dicha composicion de combustible se introduce, dicho tratamiento incluye la separacion física del componente de hidrocarburo de la fase de adsorcion o fase de adsorcion de metal. Preferiblemente el nivel de depositos en el motor luego del funcionamiento del mismo con dicha composicion de combustible en el motor es menor que el nivel de depositos en el motor luego del funcionamiento del motor con composicion de combustible alternativa en el motor, dicha composicion de combustible alternativa tiene esencialmente las mismas características que la composicion de combustible pero el componente hidrocarburo no fue tratado con dicho material absorbente o metal adsorbente.
    • 30. 发明专利
    • COMPOSICIONES DE GASOLINA
    • AR038357A1
    • 2005-01-12
    • ARP030010042
    • 2003-02-10
    • SHELL INT RESEARCH
    • CLAYTON CHRISTOPHER WILLIAMKENDALL DAVID ROYMARTIN DAVID PHILIPPRICE RICHARD JOHN
    • C10L1/14C10L1/16C10L1/18C10L1/22
    • La presente presenta una composición de gasolina con una concentración mayoritaria de gasolina adecuada para utilizar en un motor de encendido de chispa; 5 a 1000 ppmw, basado en la composición total, de una sal de ácido graso de una oligoamina alcoxilada de fórmula general (1) en la que cada unidad A representa independientemente un grupo alquileno C2-8, cada unidad R representa independientemente un alquilo C7-23 ó grupos alquenilos únicos ó múltiples no saturados C7-23, opcionalmente sustituido por uno ó más grupos -OH, cada unidad Z representa independientemente un grupo alquileno C1-8, un grupo cicloalquileno C3-8 ó un grupo arileno ó arilalquileno C6-12; m representa 0 ó un numero entero de 1 a 5, y el total de todas las variables x suma 50% a 300% de (m+3); y 600 a 2000 ppmw, en base a la composición total de un coaditivo seleccionado de un grupo que consiste en (a) un detergente de nitrógeno con un grupo hidrocarburo univalente con un peso molecular promedio (Mn) en el rango de 750 a 6000; (b) una polialfaolefina con una viscosidad a 100°C en el rango de 2 x 10-6 a 2 x 10-5 m2/s (2 a 20 centistokes), el oligómero C18-80 deriva de al menos un monómero alfaolefínico C8-16; (c) un compuesto polioxialquileno seleccionado de glicoles, mono- y diéteres de los mismos, con un peso molecular promedio (Mn) en el rango de 400 a 3000; y mezclas de cualquiera de los dos ó de los tres (a), (b) y (c).