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    Hydroconversion of heavy feeds by use of both supported and unsupported catalysts
    41.
    发明授权
    Hydroconversion of heavy feeds by use of both supported and unsupported catalysts 失效
    通过使用载体和未负载的催化剂对重质进料进行加氢转化

    公开(公告)号：US5108581A

    公开(公告)日：1992-04-28

    申请号：US607928

    申请日：1990-11-01

    Applicant: Clyde L. Aldridge ,  Roby Bearden, Jr. ,  William E. Lewis

    Inventor： Clyde L. Aldridge ,  Roby Bearden, Jr. ,  William E. Lewis

    IPC: C10G1/08

    CPC classification number: C10G1/086

    Abstract: Disclosed is a catalytic process for hydroconverting heavy hydrocarbonaceous feedstocks to lower boiling products wherein a catalyst precursor concentrate or catalyst concentrate is first prepared in a heavy oil medium then fed to a hydroconversion zone which may also contain a supported hydrotreating catalyst. The hydroconversion zone may be operated in either slurry or ebullating bed mode.

    Abstract translation: 公开了一种用于将重质烃原料加氢转化成低沸点产物的催化方法，其中首先在重油介质中制备催化剂前体浓缩物或催化剂浓缩物，然后将其加入到还可以含有负载型加氢处理催化剂的加氢转化区。 加氢转化区可以以浆料或沸腾床模式操作。

    Staged slurry hydroconversion process
    42.
    发明授权
    Staged slurry hydroconversion process 失效
    分级浆液加氢转化法

    公开(公告)号：US4151070A

    公开(公告)日：1979-04-24

    申请号：US862341

    申请日：1977-12-20

    Applicant: David E. Allan ,  William E. Lewis

    Inventor： David E. Allan ,  William E. Lewis

    IPC: C10G49/12 ,  C10G65/02 ,  C10G13/06 ,  C10G37/02

    CPC classification number: C10G49/12 ,  C10G65/02

    Abstract: A staged hydrocarbon hydroconversion process is provided in which a portion of the product boiling up to an atmospheric pressure distillation cut point of about 1050.degree. F. is removed between the stages and in which the first stage is operated at lower severity than the second stage.

    Abstract translation: 提供了分阶段的烃加氢转化方法，其中沸腾至大约1050°F的大气压蒸馏馏分的产物的一部分在阶段之间被除去，其中第一阶段以比第二阶段更低的严重程度运行。

    Co-processing of diesel biofeed and heavy oil
    47.
    发明授权
    Co-processing of diesel biofeed and heavy oil 有权
    柴油生物饲料和重油的协同加工

    公开(公告)号：US08632675B2

    公开(公告)日：2014-01-21

    申请号：US12653459

    申请日：2009-12-15

    Applicant: Kathryn Y. Cole ,  William E. Lewis

    Inventor： Kathryn Y. Cole ,  William E. Lewis

    IPC: C10G65/04 ,  C10G65/10 ,  C10G45/02

    CPC classification number: C10G45/64 ,  C10G65/12 ,  C10G69/02 ,  C10G2300/1011 ,  C10G2300/202 ,  C10G2400/04 ,  C10G2400/10 ,  Y02P30/20

    Abstract: Processes are provided for producing a diesel fuel product having a sulfur content of 10 ppm by weight or less from feed sources that include up to 50% by weight of a biocomponent feedstock. The biocomponent feedstock is co-processed with a heavy oil feed in a severe hydrotreating stage. The product from the severe hydrotreatment stage is fractionated to separate out a diesel boiling range fraction, which is then separately hydrotreated.

    Abstract translation: 提供了用于生产具有包含至多50重量％的生物组分原料的进料源的硫含量为10重量ppm以下的柴油燃料产品的方法。 生物组分原料在重质加氢处理阶段与重油进料共处理。 将来自严重加氢处理阶段的产物分馏以分离柴油沸程馏分，然后分别加氢处理。

    Hydrocracker post-treat catalyst for production of low sulfur fuels
    49.
    发明申请
    Hydrocracker post-treat catalyst for production of low sulfur fuels 有权
    用于生产低硫燃料的加氢裂化器后处理催化剂

    公开(公告)号：US20070278135A1

    公开(公告)日：2007-12-06

    申请号：US11446251

    申请日：2006-06-02

    Applicant: William J. Tracy ,  Chuansheng Bai ,  Robert A. Bradway ,  William E. Lewis ,  Randolph J. Smiley

    Inventor： William J. Tracy ,  Chuansheng Bai ,  Robert A. Bradway ,  William E. Lewis ,  Randolph J. Smiley

    IPC: C10G65/00 ,  C10G69/00

    CPC classification number: C10G65/12 ,  B01J23/883 ,  B01J23/8885 ,  B01J31/10 ,  C10G45/08

    Abstract: A hydrocracking process for converting a petroleum feedstock to higher gravity, lower sulfur products, especially ultra low sulfur road diesel fuel. The process may be operated as a single-stage or two-stage hydrocracking. In each case, a hydrocracking step is followed directly by a post-treat hydrodesulfurization zone using a bulk multimetallic catalyst comprised of at least one Group VIII non-noble metal and at least two Group VIB metals with a ratio of Group VIB metal to Group VIII non-noble metal is from about 10:1 to about 1:10. In the two-stage option with interstage ammonia removal, the initial hydrocracking step may be followed by hydrodesulfurization using the bulk multimetallic catalyst prior to the ammonia removal which is followed by the second hydrocracking step. A final hydrodesulfurization over the bulk multimetallic catalyst may follow. The hydrodesulfurization over the bulk multimetallic catalyst is carried out at a pressure of at least 25 barg and preferably at least 40 barg.

    Abstract translation: 用于将石油原料转化为更高重力，较低硫产物，特别是超低硫道路柴油的加氢裂化方法。 该方法可以作为单级或两级加氢裂化操作。 在每种情况下，加氢裂化步骤直接通过后处理加氢脱硫区，使用由至少一种VIII族非贵金属和至少两种VIB族金属与VIII族的VIB族金属组成的本体多金属催化剂 非贵金属为约10:1至约1:10。 在阶段氨除去的两阶段选择中，初始加氢裂化步骤之后可以在除氨之前使用大量多金属催化剂进行加氢脱硫，其后是第二加氢裂化步骤。 可以遵循大量多金属催化剂的最终加氢脱硫。 本体多金属催化剂上的加氢脱硫在至少25barg，优选至少40barg的压力下进行。

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