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    CONVERSION OF LIGHT NAPHTHA TO ENHANCED VALUE PRODUCTS IN AN INTEGRATED REACTOR PROCESS
    75.
    发明申请
    CONVERSION OF LIGHT NAPHTHA TO ENHANCED VALUE PRODUCTS IN AN INTEGRATED REACTOR PROCESS 有权

    公开(公告)号：US20220389334A1

    公开(公告)日：2022-12-08

    申请号：US17338863

    申请日：2021-06-04

    申请人： Saudi Arabian Oil Company

    发明人： Omer Refa Koseoglu ,  Yaming Jin

    IPC分类号： C10G59/02 ,  C10G61/02 ,  C10G35/09 ,  C10G35/095

    摘要： An integrated process for conversion of a hydrocarbon stream comprising light naphtha to enhanced value products. The process includes passing the hydrocarbon stream through the first reactor, the first reactor being an isomerization reactor with an isomerization catalyst disposed therein to generate an isomerate stream comprising at least 20% by weight iso-paraffins. The process further includes passing the isomerate from the first reactor through a second reactor, the second reactor being an aromatization reactor with an aromatization catalyst disposed therein to generate an aromatic rich stream. The process finally includes passing the aromatic rich stream to an aromatic recovery complex to separate the aromatic rich stream into an aromatic fraction, a raffinate fraction comprising unconverted paraffins, and an aromatic bottoms fraction comprising C9+ hydrocarbons, where the aromatic fraction comprises benzene, toluene and mixed xylenes. An associated system for performing the process is also provided.

    Staged fluid catalytic cracking processes incorporating a solids separation device for upgrading naphtha range material
    76.
    发明授权
    Staged fluid catalytic cracking processes incorporating a solids separation device for upgrading naphtha range material 有权

    公开(公告)号：US11377602B2

    公开(公告)日：2022-07-05

    申请号：US16838506

    申请日：2020-04-02

    申请人： LUMMUS TECHNOLOGY LLC

    发明人： Bryan Tomsula ,  Liang Chen ,  Peter Loezos ,  Rama Rao Marri

    IPC分类号： C10G61/02 ,  B01J8/18 ,  B01J8/26 ,  B03B5/32

    摘要： Processes and systems for the conversion of hydrocarbons herein may include separating an effluent from a moving bed reactor, the effluent including reaction product, first particulate catalyst, and second particulate catalyst. The separating may recover a first stream including the reaction product and first particulate catalyst and a second stream including second particulate catalyst. The second stream may be admixed with a regenerated catalyst stream including both first and second particulate catalyst at an elevated temperature. The admixing may produce a mixed catalyst at a relatively uniform temperature less than the elevated regenerated catalyst temperature, where the temperature is more advantageous for contacting light naphtha and heavy naphtha within the moving bed reactor to produce the effluent including the reaction product, the first particulate catalyst, and the second particulate catalyst.

    Process for converting C2—C5 hydrocarbons to gasoline and diesel fuel blendstocks
    77.
    发明授权
    Process for converting C2—C5 hydrocarbons to gasoline and diesel fuel blendstocks 有权

    公开(公告)号：US10941357B2

    公开(公告)日：2021-03-09

    申请号：US16386190

    申请日：2019-04-16

    申请人： Swift Fuels, LLC

    发明人： Chris D'Acosta ,  Jeffery Miller ,  Kurtis Sluss ,  Benjamin Wegenhart

    IPC分类号： C10G59/04 ,  C10G61/02 ,  C10L10/12 ,  C10L1/06 ,  C10L1/08

    摘要： Disclosed is a process for converting C2-5 alkanes to higher-value C5-24+ hydrocarbon fuels and fuel blendstocks including reacting the C2-5 alkanes in a thermal olefination reactor operating at a temperature, pressure and space velocity to convent the alkanes to olefins and in the absence of both a dehydrogenation catalyst and steam. At least a portion of the product olefin stream is oligomerized using a zeolite catalyst to crack, oligomerize and cyclize the product olefins to form the fuel products, which are then recovered. The process is useful in removing sulfur and nitrogen-based compounds in a single step process, while reducing total costs of processing and eliminating the need for additives used in the field.

    SUPERCRITICAL WATER PROCESS TO PRODUCE BOTTOM FREE HYDROCARBONS
    78.
    发明申请
    SUPERCRITICAL WATER PROCESS TO PRODUCE BOTTOM FREE HYDROCARBONS 有权

    公开(公告)号：US20210002565A1

    公开(公告)日：2021-01-07

    申请号：US17025307

    申请日：2020-09-18

    申请人： Saudi Arabian Oil Company

    发明人： Ki-Hyouk Choi ,  Bader Alotaibi ,  Mohammad Garhoush

    IPC分类号： C10G61/02 ,  B01J3/00

    摘要： A process to produce a light hydrocarbon fraction from a heavy residue feed, the process comprising the steps of operating the first supercritical reactor such that the heavy residue feed and the supercritical water stream undergo conversion reactions to produce a reactor effluent, introducing the reactor effluent to a top inlet in a top portion of a second supercritical reactor, introducing a supercritical water stream to a bottom inlet in a bottom portion of the second supercritical reactor, operating the second supercritical reactor such that the bottom of the barrel fraction is configured to settle in the bottom portion of the second supercritical reactor, withdrawing an upgraded product stream from a top outlet in the top portion of the second supercritical reactor, and withdrawing a heavy product stream from a bottom outlet in the bottom portion of the second supercritical reactor.

    Process for increasing hydrocarbon yield from catalytic reformer
    79.
    发明授权
    Process for increasing hydrocarbon yield from catalytic reformer 有权

    公开(公告)号：US10557091B2

    公开(公告)日：2020-02-11

    申请号：US15601871

    申请日：2017-05-22

    申请人： UOP LLC

    发明人： Ka L. Lok ,  Bryan K. Glover ,  Alexander V. Sabitov ,  Jeffrey R. Grott

    IPC分类号： C10G63/02 ,  C10G59/04 ,  C10G61/02 ,  C10G35/10

    摘要： A reforming reactor and process of using same in which residence time of feed within a chamber of a reactor is shortened. Feed is injected into the reactor into a non-reactive zone. The non-reactive zone has two portions, a first portion receiving the feed, and a second portion receiving a purge gas. The purge gas will flow from the second portion to the first portion to prevent flow of the feed from the first portion to the second portion. The combined gas may be passed to a reaction zone for catalytic reforming. The first portion and the second portion may be separated by a baffle.