PROCESS FOR POLYMER MIXTURE HYDROCONVERSION
    4.
    发明申请

    公开(公告)号:WO2020129020A1

    公开(公告)日:2020-06-25

    申请号:PCT/IB2019/061213

    申请日:2019-12-20

    摘要: The present invention relates to a process for the hydroconversion of mixtures of polymers or plastics which comprises the pre-treatment of the mixtures through methods selected from mechanical methods, chemical methods, thermal methods, or combinations thereof forming a pre-treated charge. The pre-treated charge is mixed with a hydrocarbon vacuum residue, optionally pre-heated, to form a reactant mixture. The reactant mixture is fed to a hydroconversion section in slurry phase, together with a catalyst precursor containing Molybdenum, and a stream containing hydrogen, forming a reaction effluent. The effluent is separated into at least one high-pressure and high-temperature separator in a vapour phase and a slurry phase. The separate vapour phase is sent to a gas treatment section with the function of separating a liquid fraction from the gas containing hydrogen and hydrocarbon gases having from 1 to 4 carbon atoms; said liquid fraction comprising naphtha, atmospheric gas oil (AGO), vacuum gas oil (VGO). The slurry phase is then sent to a separation section that has the function of separating the fractions of the Vacuum Gas Oil (VGO), Heavy Vacuum Gas Oil (HVGO), Light Vacuum Gas Oil (LVGO), Atmospheric Gas Oil (AGO), from a stream of heavy organic products which contains asphaltenes, unconverted charge, catalyst and solid formed during the hydroconversion reaction. This stream of heavy organic products is partly recirculated to the hydroconversion section and partly forms a purge stream.

    AN EBULLATED BED PROCESS FOR HIGH CONVERSION OF HEAVY HYDROCARBONS WITH A LOW SEDIMENT YIELD
    8.
    发明申请
    AN EBULLATED BED PROCESS FOR HIGH CONVERSION OF HEAVY HYDROCARBONS WITH A LOW SEDIMENT YIELD 审中-公开
    低沉积物产量的重烃高沸腾床工艺

    公开(公告)号:WO2017189390A1

    公开(公告)日:2017-11-02

    申请号:PCT/US2017/029048

    申请日:2017-04-24

    IPC分类号: C10G47/00 C10G47/26

    摘要: An ebullated bed process for the hydroconversion of heavy hydrocarbon feedstocks that provides for high conversion of the heavy hydrocarbon with a low sediment yield. The process uses for its catalyst bed small particles of a specifically defined shaped hydroprocessing catalyst which is contacted with the heavy hydrocarbon feedstock under hydroconversion conditions and yields a hydrocarbon conversion having a relatively low sediment content.

    摘要翻译: 用于重质烃原料的加氢转化的沸腾床方法提供具有低沉积物产率的重质烃的高转化率。 该方法使用其催化剂床的小颗粒的特定形状的加氢处理催化剂,其在加氢转化条件下与重质烃原料接触并产生具有相对低的沉积物含量的烃转化率。

    METHODS AND SYSTEMS FOR SLURRY HYDROCRACKING WITH REDUCED FEED BYPASS
    10.
    发明申请
    METHODS AND SYSTEMS FOR SLURRY HYDROCRACKING WITH REDUCED FEED BYPASS 审中-公开
    用于减少进料旁路的浆料水解的方法和系统

    公开(公告)号:WO2016040270A1

    公开(公告)日:2016-03-17

    申请号:PCT/US2015/048856

    申请日:2015-09-08

    申请人: UOP LLC

    IPC分类号: C10G47/02 C10G47/26

    摘要: Methods and systems for slurry hydrocracking with reduced feed bypass and methods for modulating an amount of toluene insoluble material present in a slurry hydrocracking reactor are provided. An exemplary slimy hydrocracking method comprises the steps of: combining a hydrocarbon feed and a slurry hydrocracking catalyst or catalyst precursor to generate a slurry hydrocracking feed; introducing the slurry hydrocracking feed to a slurry hydrocracking reactor under hydrocracking conditions suitable to generate a first product stream; drawing a drag stream from the slurry hydrocracking reactor, the drag stream comprising a hydrocarbon, mesophase material, and solid catalyst particles; separating the drag stream into a first separated stream and a recycle stream, with the first separated stream comprising mesophase material and solid catalyst particles, and the recycle stream comprising the hydrocarbon; and directing the recycle stream into the slurry hydrocracking reactor.

    摘要翻译: 提供了用于减少进料旁路的浆料加氢裂化的方法和系统以及用于调节存在于浆料加氢裂化反应器中的量的甲苯不溶物的方法。 示例性的粘性加氢裂化方法包括以下步骤:组合烃进料和浆料加氢裂化催化剂或催化剂前体以产生浆料加氢裂化原料; 在适于产生第一产物流的加氢裂化条件下将淤浆加氢裂化原料引入浆料加氢裂化反应器; 从浆料加氢裂化反应器中抽出阻力流,所述拖曳流包含烃,中间相材料和固体催化剂颗粒; 将所述拖曳流分离成第一分离流和循环流,其中所述第一分离流包含中间相材料和固体催化剂颗粒,并且所述循环流包含所述烃; 并将再循环流引导到浆料加氢裂化反应器中。