PROCESS FOR PRODUCING VARIOUS VISCOSITY GRADES OF BITUMEN
    26.
    发明申请
    PROCESS FOR PRODUCING VARIOUS VISCOSITY GRADES OF BITUMEN 审中-公开
    生产各种各样的粘度等级的工艺

    公开(公告)号:US20150166903A1

    公开(公告)日:2015-06-18

    申请号:US14414408

    申请日:2013-07-12

    CPC classification number: C10G53/04 C08L91/00 C08L95/00 C08L2555/74 C10G53/06

    Abstract: The present invention relates to an aromatic enriched deasphalted oil extract fraction for preparing bitumen. The present invention also relates to a process for preparing the aromatic enriched deasphalted oil extract fraction for preparing bitumen. The present invention further relates to bitumen and process for preparing the bitumen using the aromatic enriched deasphalted oil extract fraction. The aromatic enriched deasphalted oil extract fraction obtained in accordance with the present invention can be used preparing plurality of grades of bitumen. Also, bitumen obtained in accordance with the present invention contains extremely low concentration of poly cyclic aromatics and more particularly benzo(a)pyrene.

    Abstract translation: 本发明涉及一种用于制备沥青的芳香族富集脱沥青油提取物馏分。 本发明还涉及制备用于制备沥青的富含芳烃的脱沥青油提取物馏分的方法。 本发明还涉及使用富含芳烃的脱沥青油提取物馏分制备沥青的沥青和方法。 根据本发明获得的富含芳烃的脱沥青油提取物组分可用于制备多种级别的沥青。 此外,根据本发明获得的沥青含有极低浓度的多环芳族化合物,更特别地苯并(a)芘。

    Process intensification in hydroprocessing

    公开(公告)号:US10017703B2

    公开(公告)日:2018-07-10

    申请号:US14313783

    申请日:2014-06-24

    CPC classification number: C10G65/04 C10G2300/202

    Abstract: A multi-stage hydrotreating process obtains ultra-low sulfur diesel boiling range hydrocarbon having less than 10 ppm sulfur with elimination of external hot high pressure separator and avoids the formation of recombinant mercaptans by removing excess hydrogen sulfide formed during hydroprocessing reaction. The process includes mixing a diesel boiling range hydrocarbon feedstock with hydrogen and sending to the first predominantly liquid phase hydroprocessing reaction stage. Effluent from the first hydroprocessing reaction stage is sent to first separator zone of open and empty space in the upper part of the second hydroprocessing reaction stage to flash off the dissolved reaction products hydrogen sulfide and ammonia. Liquid part of the effluent of first hydroprocessing reaction stage is passed to the second predominantly liquid phase hydroprocessing reaction stage. The process is repeated until the liquid product sulfur level of less than 10 ppm is attained and the liquid product is sent to further processing.

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