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    Configuring multiple catalytic beds
    142.
    发明授权
    Configuring multiple catalytic beds 有权

    公开(公告)号：US10811121B2

    公开(公告)日：2020-10-20

    申请号：US15891680

    申请日：2018-02-08

    Applicant: PHILLIPS 66 COMPANY

    Inventor： Alexandru Platon ,  Edgar Lotero Alegria

    IPC: G16C20/10 ,  B01J8/04 ,  G06F17/17 ,  B01J8/00

    Abstract: The present disclosure relates generally to methods and systems for achieving enhanced catalytic performance via the strategic arrangement of multiple catalyst beds in series, where each catalyst bed comprises a compositionally-distinct catalyst, and each catalyst facilitates the conversion of the same structural moieties on the reactant to form the same product. Arranging multiple catalyst beds according to the methods and systems disclosed herein allows a predictable enhancement of conversion of the reactant to product without the need for time-consuming experimentation to test all possible catalysts configurations.

    HYDROCRACKING PROCESS FOR PRODUCING DISTILLATE OR NAPTHA
    146.
    发明申请
    HYDROCRACKING PROCESS FOR PRODUCING DISTILLATE OR NAPTHA 审中-公开

    公开(公告)号：US20200181511A1

    公开(公告)日：2020-06-11

    申请号：US16710213

    申请日：2019-12-11

    Applicant: PHILLIPS 66 COMPANY

    Inventor： Xiangxin Yang

    IPC: C10G65/12 ,  C10G47/36 ,  C10G47/10

    Abstract: The invention relates to a catalytic hydrocracker with two different catalyst beds within the reactor where each is loaded with a catalyst that has different hydrocracking properties. A first catalyst bed preferably cracks heavy oil more aggressively than the catalyst in the second bed. The catalytic hydrocracker includes further two recycle lines such that one directs unconverted oil through both hydrocracker beds and a bypass inlet is positioned between the first and second catalyst beds to admit unconverted oil to pass only through the second less aggressive hydrocracker catalyst bed. When gasoline prices favor the production of gasoline, less unconverted oil is recycled through the bypass therefore making more gasoline, but when prices favor the production of jet and diesel, more recycle is directed through the bypass recycle thus making less gasoline and more diesel and jet fuel.

    COMPOSITE CARBON-CARBON PARTICLES
    147.
    发明申请
    COMPOSITE CARBON-CARBON PARTICLES 审中-公开

    公开(公告)号：US20200172402A1

    公开(公告)日：2020-06-04

    申请号：US16209609

    申请日：2018-12-04

    Applicant: PHILLIPS 66 COMPANY

    Inventor： Zhenhua Mao

    IPC: C01B32/205 ,  C01B32/215 ,  C01B32/23 ,  H01M4/1393

    Abstract: Carbon particles are coated with a water-soluble carbon residue material by oxidizing the carbon residue in water and forming a solid coating on the particles. The coated particles may be heated to graphite forming temperatures to prepare the coated particles for use an anode powder for a battery.

    IMMISCIBLE LIQUID SEPARATED BATTERY SYSTEM
    148.
    发明申请
    IMMISCIBLE LIQUID SEPARATED BATTERY SYSTEM 审中-公开

    公开(公告)号：US20200099081A1

    公开(公告)日：2020-03-26

    申请号：US16578124

    申请日：2019-09-20

    Applicant: PHILLIPS 66 COMPANY

    Inventor： James Anthony Suttil ,  Hongjin Tan ,  Neal McDaniel ,  Sharmila Samaroo ,  Jeffrey H. Drese

    IPC: H01M8/18 ,  H01M6/14

    Abstract: A redox flow battery is described that does not include an ion exchange resin such as a proton exchange membrane but rather uses a generally stationary separator liquid that separates the anolyte from the catholyte at immiscible liquid-liquid interfaces. Solvents and electrochemically active components of the anolyte and catholyte would not cross the liquid-liquid interfaces between the separator liquid and the anolyte and catholyte, but certain ions in each of the anolyte and catholyte would cross the interface during charging and discharging of the redox flow battery. The separator liquid comprises a relatively small total volume of liquid in such a flow battery arrangement as compared to the anolyte and catholyte. Suitable chemical options are described along with system options for utilizing immiscible phases.

    Skimmer blocker
    149.
    发明授权
    Skimmer blocker 有权

    公开(公告)号：US10553082B2

    公开(公告)日：2020-02-04

    申请号：US15078573

    申请日：2016-03-23

    Applicant: Phillips 66 Company

    Inventor： Gary S. Brush

    IPC: G07F19/00 ,  G06K7/01

    Abstract: The invention relates to blocking fraudulent gathering of credit card and debit card information during a legitimate payment transaction at a credit/debit card reader. The invention includes the installation, preferably in a non-uniform manner, of blockers onto one or more faces or surfaces of the card reader. Properly installed blockers will tend to prevent the easy installation of a flush mounted skimmer device that is designed to overlay the legitimate card reader at a store or point of sale location such as a gasoline pump.

    SYSTEMS FOR CATALYTIC ACTIVATION OF ISOPENTANE-ENRICHED MIXTURES
    150.
    发明申请
    SYSTEMS FOR CATALYTIC ACTIVATION OF ISOPENTANE-ENRICHED MIXTURES 审中-公开

    公开(公告)号：US20190300805A1

    公开(公告)日：2019-10-03

    申请号：US16364836

    申请日：2019-03-26

    Applicant: PHILLIPS 66 COMPANY

    Inventor： Anthony O. Baldridge ,  Neal D. McDaniel ,  James A. Suttil ,  Soumen Kundu ,  Jianhua Yao ,  Bruce B. Randolph ,  Mazi Sardashti ,  Steven E. Lusk ,  Robert M. Walston

    IPC: C10G69/12 ,  C10G5/06 ,  C10G45/64

    Abstract: The present disclosure relates generally to systems operable to produce liquid transportation fuels by converting a hydrocarbon feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. The system separates the hydrocarbon feed stream to form a first fraction comprising isopentane and smaller hydrocarbons, and a second fraction comprising n-pentane and larger components of the hydrocarbon feeds stream. Each fraction is then catalytically-activated in a separate activation reactor containing a separate activation catalyst, where the conditions maintained in each reactor are selected to maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first activation reactor is maintained at a lower temperature than the second activation reactor. Certain embodiments of the system mix at least a portion of the effluents from the first and second activation reactor and convert the resulting mixed effluent in either an oligomerization reactor containing an oligomerization catalyst or an oligomerization reactor containing an alkylation catalyst to provide enhanced yields of upgraded hydrocarbon products that are characterized as a liquid transportation fuel or a blend component thereof.

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