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    TYPE II FATTY ACID SYSTHESIS ENZYMES IN REVERSE B-OXIDATION
    81.
    发明公开
    TYPE II FATTY ACID SYSTHESIS ENZYMES IN REVERSE B-OXIDATION 审中-公开
    TYP-II-FETsÄYSYNTHESEENZYMEIN DER REVERSE-B-OXIDATION

    公开(公告)号：EP3099763A1

    公开(公告)日：2016-12-07

    申请号：EP15740946.7

    申请日：2015-01-26

    Applicant: William Marsh Rice University

    Inventor： GONZALEZ, Ramon ,  CLOMBURG, James, M. ,  VICK, Jacob, E.

    IPC: C10L1/06

    CPC classification number: C12P7/64 ,  C10L1/02 ,  C10L1/04 ,  C12N9/00 ,  C12N9/0006 ,  C12N9/0008 ,  C12N9/001 ,  C12N9/0071 ,  C12N9/1029 ,  C12N9/1096 ,  C12N9/88 ,  C12N15/52 ,  C12Y101/011 ,  C12Y101/03013 ,  C12Y102/01 ,  C12Y102/01003 ,  C12Y103/01009 ,  C12Y114/00 ,  C12Y203/01009 ,  C12Y206/00 ,  C12Y401/99005 ,  C12Y402/01059 ,  Y02E50/343

    Abstract: This disclosure describes enzymes from the type II (a discrete set of enzymes) fatty acid synthesis ("FAS") pathway that can be used in combination with thiolases to operate a functional reversal of the β-oxidation cycle. A combination of thiolases with one or more of 3-oxoacyl-[acyl-carrier-protein] reductase (FabG, others), 3-hydroxyacyl-[acp] dehydratase (FabA, FabZ, others), and enoyl-[acyl-carrier-protein] reductase (FabI, FabK, FabL, FabV, others) yields a functional reversal of the β-oxidation cycle. If only one or two enzymes are used, the remaining enzymes will be traditional beta oxidation enzymes. Once this cycle is coupled with the appropriate priming and termination pathways, the production of carboxylic acids, alcohols, hydrocarbons, amines and their α-, β-, and ω-functionalized derivatives from renewable carbon sources can be achieved.

    Abstract translation: 本公开描述了可以与硫醇酶组合使用以操作β-氧化循环的功能性逆转的来自II型（一组离散酶）脂肪酸合成（“FAS”）途径的酶。 硫氧酶与一个或多个3-氧基酰基 - [酰基 - 载体 - 蛋白]还原酶（FabG，其他），3-羟基酰基 - [acp]脱水酶（FabA，FabZ等）和烯酰基 - - 蛋白]还原酶（FabI，FabK，FabL，FabV等）产生β-氧化循环的功能逆转。 如果只使用一种或两种酶，剩余的酶将是传统的β氧化酶。 一旦这个循环与适当的引发和终止途径相结合，就可以实现羧酸，醇，烃，胺及其可再生碳源的α-，β-和ω官能化衍生物的生产。

    ENHANCEMENT OF FISCHER-TROPSCH PROCESS FOR HYDROCARBON FUEL FORMULATION IN A GTL ENVIRONMENT
    86.
    发明公开
    ENHANCEMENT OF FISCHER-TROPSCH PROCESS FOR HYDROCARBON FUEL FORMULATION IN A GTL ENVIRONMENT 审中-公开
    在GTL环境中加强烃类燃料配方的费歇尔 - 托普索法

    公开(公告)号：EP2847301A1

    公开(公告)日：2015-03-18

    申请号：EP13787536.5

    申请日：2013-05-06

    Applicant: Expander Energy Inc.

    Inventor： KRESNYAK, Steve ,  WAGNER, Jan ,  PRICE, Steve

    IPC: C10G50/00 ,  C10L3/10 ,  C10K1/00 ,  C10L1/06 ,  C10L1/08

    Abstract: An enhanced natural gas processing method using Fischer-Tropsch (FT) process for the synthesis of sulfur free, clean burning, hydrocarbon fuels, examples of which include syndiesel and aviation fuel. A selection of natural gas, separately or combined with portions of natural gas liquids and FT naphtha and FT vapors are destroyed in a syngas generator and used or recycled as feedstock to an Fischer-Tropsch (FT) reactor in order to enhance the production of syndiesel from the reactor. The process enhancement results is the maximum production of formulated syndiesel without the presence or formation of low value by-products.

    Abstract translation: 采用费托（FT）工艺合成无硫清洁燃烧碳氢燃料的增强型天然气处理方法，其实例包括合成柴油和航空燃料。 单独或与天然气液体和FT石脑油和FT蒸汽的一部分组合的天然气的选择在合成气发生器中被破坏并且作为原料被使用或再循环至费 - 托（FT）反应器以增强合成气生产 来自反应堆。 过程增强结果是在不存在或形成低价值副产物的情况下最大化配制的合成柴油的生产。

    PRODUCTION OF LIQUID HYDROCARBONS
    87.
    发明公开
    PRODUCTION OF LIQUID HYDROCARBONS 审中-公开
    HERSTELLUNGFLÜSSIGERKOHLENWASSERSTOFFE

    公开(公告)号：EP2834326A1

    公开(公告)日：2015-02-11

    申请号：EP13718037.8

    申请日：2013-04-05

    Applicant: IGTL Technology Ltd

    Inventor： HYMAN, Richard John

    IPC: C10G35/04 ,  C10G45/58 ,  C10L1/06 ,  C10L1/08

    CPC classification number: C10L1/04 ,  C10G2/332 ,  C10G2/343 ,  C10G35/04 ,  C10G45/58 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  C10G2400/20 ,  C10L1/06 ,  C10L1/08 ,  C10L2200/0438 ,  C10L2200/0446 ,  C10L2200/0492 ,  C10L2270/023 ,  C10L2270/026

    Abstract: The invention relates to a process for the conversion of hydrogen and one or more oxides of carbon to hydrocarbons, which process comprises: contacting hydrogen and one or more oxides of carbon with a catalyst in a reaction zone; removing from the reaction zone an outlet stream comprising unreacted hydrogen, unreacted one or more oxides of carbon and one or more hydrocarbons and feeding the outlet stream to a separation zone in which the outlet stream is divided into at least three fractions, in which; a first fraction predominantly comprises unreacted hydrogen, unreacted one or more oxides of carbon and hydrocarbons having from 1 to 4 carbon atoms; a second fraction predominantly comprises hydrocarbons having 5 to 9 carbon atoms, at least a portion of which hydrocarbons having from 5 to 9 carbon atoms are olefinic; and a third fraction predominantly comprises hydrocarbons having 10 or more carbon atoms; characterised in that at least a portion of the second fraction is recycled to the reaction zone.

    Abstract translation: 本发明涉及一种将氢和一种或多种碳氧化物转化成烃的方法，该方法包括：使氢和一种或多种碳氧化物与反应区中的催化剂接触; 从反应区域除去包含未反应的氢，未反应的一种或多种碳和一种或多种烃的氧化物的出口物流，并将出口物流输送到分离区，其中出口物流被分成至少三个馏分。 第一级分主要包含未反应的氢，未反应的一种或多种碳和碳原子数为1至4的氧化物; 第二部分主要包含具有5至9个碳原子的烃，其中至少一部分具有5至9个碳原子的烃是烯属的; 并且第三部分主要包含具有10个或更多个碳原子的烃; 其特征在于，第二级分的至少一部分被再循环到反应区。

    METHOD FOR JOINT PRODUCTION OF LOW OCTANE NUMBER GASOLINE AND HIGH OCTANE NUMBER GASOLINE
    89.
    发明公开
    METHOD FOR JOINT PRODUCTION OF LOW OCTANE NUMBER GASOLINE AND HIGH OCTANE NUMBER GASOLINE 审中-公开
    用于汽油具有低辛烷值燃料和高辛烷值生产

    公开(公告)号：EP2641959A1

    公开(公告)日：2013-09-25

    申请号：EP11841525.6

    申请日：2011-11-15

    Applicant: Zhou, Xiangjin

    Inventor： Zhou, Xiangjin

    IPC: C10L1/06 ,  C10L1/08 ,  C10G7/00 ,  C10G53/08 ,  C07C7/12 ,  C07C7/06

    CPC classification number: C10G7/00 ,  C07C7/06 ,  C07C7/12 ,  C10G7/12 ,  C10G2300/305 ,  C10G2400/02 ,  C10L1/04 ,  C10L1/06 ,  C10L1/08 ,  C10L10/10 ,  C10L2270/023 ,  C10L2270/026 ,  C10L2290/543 ,  C07C9/21 ,  C07C9/15

    Abstract: The present invention relates to a method for joint production of low octane gasoline and high octane gasoline. In the process of oil or light oil rectification, the extraction points of the distillates therein are finely divided, and the temperature ranges for extraction of fractions are narrowed down. Each of the low and high octane components having a high content in the range from C6-C12 (which may be extended to C5-C14 where necessary) is then separately extracted. After that, low octane components are combined into compression ignition low octane gasoline products, while high octane components are combined into high octane gasoline products. The remaining fractions are respectively added as supplementing agents into the low octane gasoline products or high octane gasoline products dependent on their octane ratings. Low octane gasoline is used in compression ignition gasoline engines, while high octane gasoline is used in spark ignition gasoline engines.

    Abstract translation: 本发明涉及一种用于联合生产低辛烷值汽油和高辛烷值汽油的方法。 在油或轻油精馏过程中，其中的馏出物的提取点被细碎，并且温度范围为级分的提取被收窄。 每一个都具有在从C6-C12（其可以被扩展到C5-C14在必要时）的范围内的高含量低和高辛烷值组分的是然后分别提取。 在此之后，低辛烷值组分被组合成压缩点火低辛烷值汽油产品，而高辛烷值组分结合成高辛烷值汽油产品。 剩余的级分分别加入作为补充剂为低辛烷值汽油的产品或高辛烷值汽油产品依赖于它们的辛烷值。 低辛烷值汽油压燃式汽油发动机使用，而高辛烷值汽油的火花点火汽油发动机使用。

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