START-UP METHOD OF BUBBLE COLUMN SLURRY BED REACTOR
    3.
    发明申请
    START-UP METHOD OF BUBBLE COLUMN SLURRY BED REACTOR 有权
    泡沫柱塞式反应器的启动方法

    公开(公告)号:US20150087730A1

    公开(公告)日:2015-03-26

    申请号:US14387391

    申请日:2013-03-27

    发明人: Kazuhiko Tasaka

    IPC分类号: C07C1/04

    摘要: A start-up method of a bubble column slurry bed reactor for producing hydrocarbons includes: a first step that fills into a reactor a slurry in which a Fischer-Tropsch synthesis reaction catalyst particles are suspended in a slurry preparation oil with a 5% distillation point of 120 to 270° C., a 95% distillation point of 330 to 650° C., and a sulfur component and an aromatic component of 1 mass ppm or less, and a second step that, in a state where synthesis gas that is primarily hydrogen and carbon monoxide is introduced into the slurry filled into the reactor, raises the temperature of the reactor and starts the Fischer-Tropsch synthesis reaction. As the slurry preparation oil, one containing predetermined components in preset amounts is used. In the first step, the slurry is filled into the reactor in an amount in which airborne droplets do not flow out.

    摘要翻译: 用于生产烃的鼓泡塔淤浆床反应器的启动方法包括:第一步骤,向反应器中填充一种浆料,其中费 - 托合成反应催化剂颗粒悬浮在具有5%蒸馏点的浆料制备油中 120〜270℃,95%蒸馏点为330〜650℃,硫成分和1质量ppm以下的芳香族成分,第2工序中,在合成气为 主要将氢和一氧化碳引入填充到反应器中的浆料中,升高反应器的温度并开始费 - 托合成反应。 作为浆料制备油,使用预定量的预定组分。 在第一步骤中,将浆料以空气中的液滴不会流出的量装入反应器中。

    PROCESS FOR PRODUCING HYDROCARBON OIL AND SYSTEM FOR PRODUCING HYDROCARBON OIL
    7.
    发明申请
    PROCESS FOR PRODUCING HYDROCARBON OIL AND SYSTEM FOR PRODUCING HYDROCARBON OIL 审中-公开
    生产烃油的方法和生产烃油的方法

    公开(公告)号:US20140377142A1

    公开(公告)日:2014-12-25

    申请号:US14478433

    申请日:2014-09-05

    IPC分类号: B01D3/00

    摘要: Hydrocarbon oil obtained by Fischer-Tropsch synthesis reaction using a slurry bed reactor holding a slurry of a liquid hydrocarbon in which a catalyst is suspended; the hydrocarbon oil is fractionated into a distilled oil and a column bottom oil containing the catalyst fine powder by a rectifying column; at least part of the column bottom oil is transferred to a storage tank, and the catalyst fine powder is sedimented to the bottom of the storage tank to capture the catalyst fine powder; a residue of the column bottom oil is transferred from the rectifying column to a hydrocracker, and/or the supernatant of the column bottom oil from which the catalyst fine powder is captured by the storage tank is transferred from the storage tank to the hydrocracker; and using the hydrocracker, the residue of the column bottom oil and/or the supernatant of the column bottom oil is hydrocracked.

    摘要翻译: 通过费托合成反应获得的烃油,其使用保持催化剂悬浮的液态烃的淤浆的淤浆床反应器; 将烃油通过精馏塔分馏成蒸馏油和含有催化剂细粉末的塔底油; 将塔底油的至少一部分转移到储罐中,并将催化剂细粉沉淀到储罐的底部以捕获催化剂细粉; 柱底油的残渣从精馏塔转移到加氢裂化器中,和/或由储罐捕获催化剂细粉末的塔底油的上清液从储罐转移到加氢裂化器; 并使用加氢裂化器,将柱底油的残余物和/或塔底油的上清液加氢裂化。