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    BIOMASS CONVERSION SYSTEMS PROVIDING integrated STABILIZATION OF A HYDROLYSATE USING A SLURRY CATALYST AND METHODS FOR USE THEREOF
    291.
    发明申请
    BIOMASS CONVERSION SYSTEMS PROVIDING integrated STABILIZATION OF A HYDROLYSATE USING A SLURRY CATALYST AND METHODS FOR USE THEREOF 审中-公开
    生物质转化系统提供使用浆料催化剂的水解产物的综合稳定性及其使用方法

    公开(公告)号：US20160237359A1

    公开(公告)日：2016-08-18

    申请号：US15138246

    申请日：2016-04-26

    Applicant: SHELL OIL COMPANY

    Inventor： Joseph Broun POWELL

    IPC: C10L1/04 ,  C10G3/00

    CPC classification number: C10L1/04 ,  C10G1/002 ,  C10G1/065 ,  C10G1/083 ,  C10G3/42 ,  C10G2300/1011 ,  C10G2300/1014 ,  C10L2200/0469 ,  C10L2290/06 ,  C10L2290/10 ,  C10L2290/12 ,  C12M21/12 ,  C12M29/18 ,  C12M29/26 ,  C13K1/02 ,  D21C3/222 ,  Y02P30/20

    Abstract: Digestion of cellulosic biomass solids to form a hydrolysate may be conducted with integrated catalytic reduction during digestion to transform soluble carbohydrates in the hydrolysate into a more stable reaction product. Such integrated catalytic reduction may be conducted using a slurry catalyst. Biomass conversion systems for performing integrated catalytic reduction can comprise: a hydrothermal digestion unit that contains a slurry catalyst capable of activating molecular hydrogen; an optional hydrogen feed line that is operatively connected to the hydrothermal digestion unit; and a fluid circulation loop comprising the hydrothermal digestion unit and a catalytic reduction reactor unit, the catalytic reduction reactor unit also containing the slurry catalyst.

    Abstract translation: 消化纤维素生物质固体以形成水解产物可以在消化过程中进行一体化催化还原，以将水解产物中的可溶性碳水化合物转化为更稳定的反应产物。 这种一体化催化还原可以使用浆料催化剂进行。 用于进行一体化催化还原的生物质转化系统可以包括：含有能够活化分子氢的浆料催化剂的水热消解装置; 可操作地连接到水热消解单元的氢供给管线; 以及包含所述水热消解单元和催化还原反应器单元的流体循环回路，所述催化还原反应器单元还含有所述浆料催化剂。

    COMPOSITION AND METHOD FOR ENHANCED HYDROCARBON RECOVERY
    292.
    发明申请
    COMPOSITION AND METHOD FOR ENHANCED HYDROCARBON RECOVERY 审中-公开
    用于增强油气回收的组合物和方法

    公开(公告)号：US20160237337A1

    公开(公告)日：2016-08-18

    申请号：US15024389

    申请日：2014-09-24

    Applicant: SHELL OIL COMPANY ,  WILLIAM MARSH RICE UNIVERSITY

    Inventor： Julian Richard BARNES ,  Clarence Alphonso MILLER ,  George Jiro HIRASAKI ,  Maura Camps PUERTO ,  Sheila Teresa DUBEY ,  Carmen Geraldine REZNIK

    IPC: C09K8/584

    CPC classification number: C09K8/584

    Abstract: The invention relates to a hydrocarbon recovery composition, which composition contains: a) a first anionic surfact ant selected from the group consisting of a propoxylated primary alcohol carboxylate and a propoxylated primary alcohol glycerol sulfonate; and b) a second anionic surfactant selected from the group consisting of a propoxylated primary alcohol carboxylate and a propoxylated primary alcohol glycerol sulfonate, and wherein the first and second anionic surfactants are different. Further, the invention relates to an injectable liquid containing the hydrocarbon recovery composition and a method for treating a hydrocarbon containing formation.

    Abstract translation: 本发明涉及一种烃回收组合物，该组合物含有：a）选自丙氧基化伯醇羧酸酯和丙氧基化伯醇甘油磺酸盐的第一阴离子表面活性剂; 和b）选自丙氧基化伯醇羧酸酯和丙氧基化伯醇甘油磺酸盐的第二阴离子表面活性剂，其中第一和第二阴离子表面活性剂是不同的。 此外，本发明涉及含有烃回收组合物的可注射液体和含烃地层的处理方法。

    PROCESS FOR THE OXIDATIVE DEHYDROGENATION OF ETHANE TO ETHYLENE
    293.
    发明申请
    PROCESS FOR THE OXIDATIVE DEHYDROGENATION OF ETHANE TO ETHYLENE 审中-公开
    乙醛氧化脱乙酰乙酸的方法

    公开(公告)号：US20160237005A1

    公开(公告)日：2016-08-18

    申请号：US15031034

    申请日：2014-10-24

    Applicant: SHELL OIL COMPANY

    Inventor： Dharmesh KUMAR ,  Ronald Jan SCHOONEBEEK

    IPC: C07C5/48 ,  C07C29/149 ,  C07C1/24 ,  C07C7/04

    CPC classification number: C07C5/48 ,  C07C1/24 ,  C07C7/04 ,  C07C29/149 ,  C07C51/215 ,  C07C11/04 ,  C07C53/08 ,  C07C31/08

    Abstract: The present invention provides a process for the oxidative dehydrogenation of ethane to ethylene, the process at least comprising the steps of: (a) providing an ethane-containing stream (10); (b) subjecting the ethane-containing stream (10) provided in step (a) to oxidative dehydrogenation, thereby obtaining a stream (20) containing at least ethylene, water and acetic acid; (c) separating acetic acid from the stream (20) obtained in step (b), thereby obtaining a concentrated acetic acid stream (60) and a first ethylene-enriched stream (40); (d) subjecting the concentrated acetic acid stream (60) obtained in step (c) to hydrogenation thereby obtaining an ethanol-containing stream (80); and (e) subjecting the ethanol-containing stream (80) obtained in step (d) to dehydration thereby obtaining a second ethylene-enriched stream (90).

    Abstract translation: 本发明提供了乙烷氧化脱氢成乙烯的方法，该方法至少包括以下步骤：（a）提供含乙烷的物流（10）; （b）使步骤（a）中提供的含乙烷物流（10）进行氧化脱氢，从而获得至少含有乙烯，水和乙酸的物流（20）; （c）从步骤（b）中获得的物流（20）中分离乙酸，由此得到浓缩乙酸物流（60）和第一乙烯富集物流（40）; （d）将步骤（c）中获得的浓缩乙酸流（60）进行氢化，从而得到含乙醇的物流（80）; 和（e）使步骤（d）中获得的含乙醇的流（80）脱水，从而获得第二个富含乙烯的流（90）。

    Biomass conversion systems having a fluid circulation loop containing a centripetal force-based separation mechanism for control of cellulosic fines and methods for use thereof
    295.
    发明授权
    Biomass conversion systems having a fluid circulation loop containing a centripetal force-based separation mechanism for control of cellulosic fines and methods for use thereof 有权
    具有包含用于控制纤维素细粒的向心力分离机构的流体循环回路的生物质转化系统及其使用方法

    公开(公告)号：US09415367B2

    公开(公告)日：2016-08-16

    申请号：US14242934

    申请日：2014-04-02

    Applicant: SHELL OIL COMPANY

    Inventor： Joseph Broun Powell

    IPC: C07C1/00 ,  B01J19/00 ,  C10G3/00 ,  C10L1/02 ,  C10G1/00 ,  C10G1/06

    CPC classification number: B01J19/0046 ,  C10G1/002 ,  C10G1/065 ,  C10G3/00 ,  C10G3/42 ,  C10G2300/1014 ,  C10L1/02 ,  Y02P30/20

    Abstract: Digestion of cellulosic biomass to produce a hydrolysate may be accompanied by the formation of cellulosic fines which may be damaging to system components. Biomass conversion systems that may address the issue of cellulosic fines may comprise a fluid circulation loop comprising: a hydrothermal digestion unit; a solids separation unit that is in fluid communication with an outlet of the hydrothermal digestion unit; where the solids separation unit comprises a centripetal force-based separation mechanism that comprises a fluid outlet and a solids outlet; and a catalytic reduction reactor unit that is in fluid communication with the fluid outlet of the centripetal force-based separation mechanism and an inlet of the hydrothermal digestion unit.

    Abstract translation: 消化纤维素生物质以产生水解产物可伴随着可能损害系统组分的纤维素细粉的形成。 可能解决纤维素细粒问题的生物质转化系统可以包括流体循环回路，包括：水热消解单元; 固体分离单元，其与所述水热消解单元的出口流体连通; 其中固体分离单元包括向心力分离机构，其包括流体出口和固体出口; 以及催化还原反应器单元，其与向心力分离机构的流体出口和水热消解单元的入口流体连通。

    PROCESS FOR THE CONVERSION OF SACCHARIDE-CONTAINING FEEDSTOCK
    297.
    发明申请
    PROCESS FOR THE CONVERSION OF SACCHARIDE-CONTAINING FEEDSTOCK 有权
    含SACCHARIDE的饲料转化过程

    公开(公告)号：US20160221903A1

    公开(公告)日：2016-08-04

    申请号：US14914393

    申请日：2014-08-29

    Applicant: SHELL OIL COMPANY

    Inventor： Evert VAN DER HEIDE ,  Pieter HUIZENGA

    IPC: C07C29/60

    CPC classification number: C07C29/60 ,  C07C29/132 ,  C07C31/202 ,  C07C31/205

    Abstract: The invention provides a process for the catalytic conversion of a saccharide-containing feedstock in a reactor, wherein saccharide-containing feedstock is provided to the reactor as a feed stream through a feed pipe and is contacted with a catalyst system in the reactor, wherein the saccharide-containing feedstock in the feed pipe is maintained at a temperature below the degradation temperature of the saccharide contained therein and a section of the wall of the reactor at the point where the feed pipe enters the reactor is cooled to a temperature below the temperature of the bulk of the reactor and the reactor contents.

    Abstract translation: 本发明提供了一种用于在反应器中催化转化含糖原料的方法，其中将含糖原料作为进料流提供给反应器，并通过进料管与反应器中的催化剂体系接触，其中 进料管中的含糖原料保持在低于其中所含的糖的降解温度的温度，并且在进料管进入反应器的点处的反应器壁的一部分被冷却到低于 大部分反应器和反应器内容物。

    COMPOSITE IONIC LIQUID CATALYST
    300.
    发明申请
    COMPOSITE IONIC LIQUID CATALYST 审中-公开
    复合离子液体催化剂

    公开(公告)号：US20160199825A1

    公开(公告)日：2016-07-14

    申请号：US14914541

    申请日：2014-08-27

    Applicant: SHELL OIL COMPANY ,  CHINA UNIVERSITY OF PETROLEUM

    Inventor： Rui ZHANG ,  Jan DE WITH ,  Peter Anton August KLUSENER ,  Zhichang LIU

    IPC: B01J31/02 ,  C07C2/58

    CPC classification number: B01J31/0284 ,  B01J31/0279 ,  B01J2231/44 ,  C07C2/58 ,  C07C2527/122 ,  C07C2527/125 ,  C07C2531/02 ,  C10G29/205 ,  C10G50/00 ,  C10G2300/1092 ,  C10G2400/02 ,  C10G2400/04 ,  C07C9/21 ,  C07C9/16

    Abstract: The present invention relates to a composite ionic liquid comprising ammonium cations and composite coordinate anions derived from two or more metal salts, wherein at least one metal salt is an aluminium salt and any further metal salt is a salt of a metal selected from the group consisting of Group IB elements of the Periodic Table, Group IIB elements of the Periodic Table and transition elements of the Periodic Table, wherein the ammonium cation is a N,N′-disubstituted imidazolium cation, the substituents independently being selected from C1-C10 alkyl, and C6-C10 aryl. The composite ionic liquid of the invention is a stable catalyst, which can suitably be used to run an ionic liquid alkylation process which produces less solids and an alkylate product comprising less organic chlorides as side products than processes known from the prior art.

    Abstract translation: 本发明涉及包含铵阳离子和衍生自两种或多种金属盐的复合配位阴离子的复合离子液体，其中至少一种金属盐是铝盐，任何其它金属盐是选自以下的金属的盐： 的元素周期表的IB族元素，元素周期表的IIB族元素和周期表的过渡元素，其中铵阳离子是N，N'-二取代的咪唑鎓阳离子，所述取代基独立地选自C 1 -C 10烷基， 和C 6 -C 10芳基。 本发明的复合离子液体是稳定的催化剂，其可适用于运行产生较少固体的离子液体烷基化方法，并且包含较少有机氯化物作为副产物的烷基化产物比现有技术已知的方法。

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