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    PROCESS OF SYNTHESIS GAS CONVERSION TO LIQUID HYDROCARBON MIXTURES USING SYNTHESIS GAS CONVERSION CATALYST AND HYDROISOMERIZATION CATALYST
    31.
    发明申请
    PROCESS OF SYNTHESIS GAS CONVERSION TO LIQUID HYDROCARBON MIXTURES USING SYNTHESIS GAS CONVERSION CATALYST AND HYDROISOMERIZATION CATALYST 审中-公开
    使用合成气转化催化剂和氢化催化剂合成气体混合物的合成方法

    公开(公告)号：US20110160315A1

    公开(公告)日：2011-06-30

    申请号：US12780672

    申请日：2010-05-14

    Applicant: Charles L. Kibby ,  Robert J. Saxton ,  Kandaswamy Jothimurugesan ,  Tapan K. Das

    Inventor： Charles L. Kibby ,  Robert J. Saxton ,  Kandaswamy Jothimurugesan ,  Tapan K. Das

    IPC: C07C1/04

    CPC classification number: C07C9/22 ,  C07C1/0435 ,  C07C5/222 ,  C07C9/16 ,  C07C2529/72

    Abstract: A process is disclosed for converting synthesis gas to a liquid hydrocarbon mixture useful as distillate fuel and/or lube base oil which is substantially free of solid wax. A synthesis gas feed is contacted with a synthesis gas conversion catalyst in an upstream bed and a hydroisomerization catalyst containing a metal promoter and an acidic component in a downstream bed within a single reactor at essentially common reaction conditions. A Fischer-Tropsch wax is formed over the synthesis gas conversion catalyst and said wax is subsequently hydroisomerized over the hydroisomerization catalyst, thereby resulting in a liquid hydrocarbon mixture having a desirable product distribution.

    Abstract translation: 公开了一种将合成气转化为可用作基本上不含固体蜡的馏出物燃料和/或润滑油基础油的液体烃混合物的方法。 合成气进料在上游床中与合成气转化催化剂和含有金属助催化剂和酸性组分的加氢异构化催化剂在基本上常见的反应条件下在单个反应器内的下游床中接触。 在合成气转化催化剂上形成费托蜡，然后所述蜡在加氢异构化催化剂上加氢异构化，从而得到具有所需产物分布的液态烃混合物。

    Fischer-Tropsch processes and catalysts using stabilized supports
    36.
    发明授权
    Fischer-Tropsch processes and catalysts using stabilized supports 有权
    费 - 托工艺和使用稳定载体的催化剂

    公开(公告)号：US07071239B2

    公开(公告)日：2006-07-04

    申请号：US10687022

    申请日：2003-10-16

    Applicant: J. Dale Ortego, Jr. ,  Kandaswamy Jothimurugesan ,  Rafael L. Espinoza ,  Kevin L. Coy ,  Beatrice C. Ortego

    Inventor： J. Dale Ortego, Jr. ,  Kandaswamy Jothimurugesan ,  Rafael L. Espinoza ,  Kevin L. Coy ,  Beatrice C. Ortego

    IPC: C07C27/00

    CPC classification number: B01J37/0207 ,  B01J21/005 ,  B01J21/04 ,  B01J21/06 ,  B01J21/12 ,  B01J23/74 ,  B01J23/8913 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1061 ,  B01J37/0205 ,  C10G2/332

    Abstract: A catalyst and method for producing hydrocarbons using a catalyst support having an improved hydrothermal stability, such as under Fischer-Tropsch synthesis conditions. The stabilized support is made by a method comprising treating a boehmite material in contact with at least one structural stabilizer. Contacting the boehmite with at least one structural stabilizer can include forming a mixture comprising the boehmite material and at the least one structural stabilizer. The mixture can be a sol or a slurry. The treating preferably includes drying or spray drying the mixture, and calcining in an oxidizing atmosphere to obtain the stabilized support. Preferred structural stabilizers can include an element, such as cobalt, magnesium, zirconium, boron, aluminum, barium, silicon, lanthanum, oxides thereof, or combinations thereof; or can include precipitated oxides, such as a co-precipitated silica-alumina.

    Abstract translation: 使用具有改进的水热稳定性的催化剂载体来制备烃的催化剂和方法，例如在费 - 托合成条件下。 通过包括处理与至少一种结构稳定剂接触的勃姆石材料的方法制备稳定的载体。 将勃姆石与至少一种结构稳定剂接触可包括形成包含勃姆石材料和至少一种结构稳定剂的混合物。 混合物可以是溶胶或浆料。 处理优选包括干燥或喷雾干燥混合物，并在氧化气氛中煅烧以获得稳定的载体。 优选的结构稳定剂可包括元素，例如钴，镁，锆，硼，铝，钡，硅，镧，氧化物或其组合; 或者可以包括沉淀氧化物，例如共沉淀二氧化硅 - 氧化铝。

    Catalyst for hydroprocessing of Fischer-Tropsch products
    37.
    发明申请
    Catalyst for hydroprocessing of Fischer-Tropsch products 审中-公开
    费 - 托产品加氢处理催化剂

    公开(公告)号：US20050274646A1

    公开(公告)日：2005-12-15

    申请号：US10866884

    申请日：2004-06-14

    Applicant: Keith Lawson ,  Kandaswamy Jothimurugesan ,  Rafael Espinoza

    Inventor： Keith Lawson ,  Kandaswamy Jothimurugesan ,  Rafael Espinoza

    IPC: B01J23/42 ,  B01J35/10 ,  B01J37/02 ,  B05D1/18 ,  B05D3/02 ,  C10G47/04 ,  C10G47/12

    CPC classification number: B01J35/10 ,  B01J23/42 ,  B01J35/1061 ,  B01J37/0211 ,  C10G47/12

    Abstract: The invention generally relates to methods for modifying a porous amorphous material comprising micropores to reduce its micropore volume and to form a support for a hydroprocessing catalyst, to methods of making said catalyst, as well as to methods for hydrocracking employing said hydroprocessing catalyst characterized by a lower selectivity towards undesirable gaseous hydrocarbon products. In one embodiment, the method for modifying the amorphous material comprises depositing an inorganic oxide or inorganic oxide precursor to the amorphous material; and treating the deposited amorphous material so as to reduce its micropore volume by at least about 5 percent, while its mean pore diameter is substantially unchanged or changed by not more than about 10 percent. Further embodiments include the amorphous material comprising silica-alumina, and the deposited inorganic oxide or inorganic oxide precursor comprising silicon.

    Abstract translation: 本发明一般涉及用于改性包含微孔以减少其微孔体积并形成用于加氢处理催化剂的载体的多孔无定形材料的方法，制备所述催化剂的方法以及使用所述加氢处理催化剂的加氢裂化方法，其特征在于 对不需要的气态烃产物的选择性降低。 在一个实施方案中，用于改性无定形材料的方法包括将无机氧化物或无机氧化物前体沉积到无定形材料中; 以及处理所沉积的非晶材料以便将其微孔体积减少至少约5％，而其平均孔径基本上不变或改变不超过约10％。 另外的实施方案包括包含二氧化硅 - 氧化铝的无定形材料和包含硅的沉积的无机氧化物或无机氧化物前体。

    Stable Support For Fischer-Tropsch Catalyst
    38.
    发明申请
    Stable Support For Fischer-Tropsch Catalyst 审中-公开
    稳定支持费托催化剂

    公开(公告)号：US20160067682A1

    公开(公告)日：2016-03-10

    申请号：US14482330

    申请日：2014-09-10

    Applicant: Kandaswamy Jothimurugesan

    Inventor： Kandaswamy Jothimurugesan

    IPC: B01J23/89 ,  C10G2/00 ,  B01J37/18 ,  B01J37/02 ,  B01J37/08

    CPC classification number: B01J23/8993 ,  B01J23/10 ,  B01J23/14 ,  B01J23/18 ,  B01J23/20 ,  B01J23/28 ,  B01J23/83 ,  B01J23/835 ,  B01J23/8435 ,  B01J23/8474 ,  B01J23/882 ,  B01J23/894 ,  B01J23/8966 ,  B01J23/8973 ,  B01J35/002 ,  B01J35/023 ,  B01J35/1038 ,  B01J35/1042 ,  B01J37/0205 ,  B01J37/024 ,  B01J37/08 ,  B01J37/18 ,  C01B2203/062 ,  C10G2/33 ,  C10G2/331 ,  C10G2/333 ,  C10G2300/70

    Abstract: A process has been developed for preparing a Fischer-Tropsch catalyst precursor and a Fischer-Tropsch catalyst made from the precursor. The process includes contacting a gamma alumina catalyst support material with a first solution containing a compound containing an element selected from the group consisting of yttrium (Y), niobium (Nb), molybdenum (Mo), tin (Sn), antimony (Sb) and mixtures thereof to obtain a modified catalyst support material. The modified catalyst support material is calcined at a temperature of at least 700° C. The calcined modified catalyst support has a pore volume of at least 0.4 cc/g. The modified catalyst support is less soluble in acid solutions than an equivalent unmodified catalyst support. The modified catalyst support is contacted with a second solution which includes a precursor compound of an active cobalt catalyst component to obtain a catalyst precursor. The catalyst precursor is reduced to activate the catalyst precursor to obtain the Fischer-Tropsch catalyst. The catalyst has enhanced hydrothermal stability as measured by losing no more than 25% of its pore volume when exposed to water vapor.

    Abstract translation: 已经开发了制备费 - 托催化剂前体和由前体制备的费 - 托催化剂的方法。 该方法包括使γ氧化铝催化剂载体材料与含有选自钇（Y），铌（Nb），钼（Mo），锡（Sn），锑（Sb） 及其混合物以获得改性的催化剂载体材料。 改性的催化剂载体材料在至少700℃的温度下煅烧。煅烧的改性催化剂载体的孔体积至少为0.4cc / g。 改性的催化剂载体在酸溶液中比相当的未改性的催化剂载体更难溶解。 将改性的催化剂载体与包含活性钴催化剂组分的前体化合物的第二溶液接触以获得催化剂前体。 催化剂前体被还原以活化催化剂前体以获得费 - 托催化剂。 催化剂具有增强的水热稳定性，当暴露于水蒸气时，其通过损失不超过其孔体积的25％来测量。

    Stable support for Fischer-Tropsch catalyst
    39.
    发明授权
    Stable support for Fischer-Tropsch catalyst 有权
    稳定支持费 - 托催化剂

    公开(公告)号：US09233360B1

    公开(公告)日：2016-01-12

    申请号：US14482313

    申请日：2014-09-10

    Applicant: Kandaswamy Jothimurugesan ,  Mark Muraoka

    Inventor： Kandaswamy Jothimurugesan ,  Mark Muraoka

    IPC: B01J21/04 ,  B01J23/75 ,  B01J23/70 ,  B01J27/185 ,  B01J23/89 ,  B01J37/02 ,  B01J37/08 ,  B01J37/18 ,  C10G2/00

    CPC classification number: B01J27/1856 ,  B01J21/04 ,  B01J23/70 ,  B01J23/75 ,  B01J23/80 ,  B01J23/8946 ,  B01J23/8953 ,  B01J23/896 ,  B01J23/8966 ,  B01J23/898 ,  B01J23/8993 ,  B01J27/188 ,  B01J27/19 ,  B01J27/198 ,  B01J35/002 ,  B01J35/1038 ,  B01J35/1042 ,  B01J37/0205 ,  B01J37/0207 ,  B01J37/024 ,  B01J37/08 ,  B01J37/18 ,  C10G2/332 ,  C10G2/333

    Abstract: A process has been developed for preparing a Fischer-Tropsch catalyst precursor and a Fischer-Tropsch catalyst made from the precursor. The process includes contacting a gamma alumina catalyst support material with a first solution containing a compound containing zinc and optionally containing P, Ti, V, Co, Ga, Ge, Mo, W and/or Pr to obtain a modified catalyst support material. The modified catalyst support material is calcined at a temperature of at least 500° C. The calcined modified catalyst support has a pore volume of at least 0.4 cc/g. The modified catalyst support is less soluble in acid solutions than an equivalent unmodified catalyst support. The modified catalyst support is contacted with a second solution which includes a precursor compound of an active cobalt catalyst component to obtain a catalyst precursor. The catalyst precursor is reduced to activate the catalyst precursor to obtain the Fischer-Tropsch catalyst. The catalyst has enhanced hydrothermal stability as measured by losing no more than 20% of its pore volume when exposed to water vapor.

    Abstract translation: 已经开发了制备费 - 托催化剂前体和由前体制备的费 - 托催化剂的方法。 该方法包括使γ氧化铝催化剂载体材料与含有锌化合物和任选地含有P，Ti，V，Co，Ga，Ge，Mo，W和/或Pr的第一溶液接触，以获得改性的催化剂载体材料。 改性的催化剂载体材料在至少500℃的温度下煅烧。煅烧的改性催化剂载体的孔体积至少为0.4cc / g。 改性的催化剂载体在酸溶液中比相当的未改性的催化剂载体更难溶解。 将改性的催化剂载体与包含活性钴催化剂组分的前体化合物的第二溶液接触以获得催化剂前体。 催化剂前体被还原以活化催化剂前体以获得费 - 托催化剂。 催化剂具有增强的水热稳定性，当暴露于水蒸气时，其通过损失其不超过其孔体积的20％来测量。

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