Process for producing liquid and, optionally, gaseous products from
gaseous reactants
    3.
    发明授权
    Process for producing liquid and, optionally, gaseous products from gaseous reactants 失效
    用于从气态反应物生产液体和任选的气态产物的方法

    公开(公告)号:US5599849A

    公开(公告)日:1997-02-04

    申请号:US187189

    申请日:1994-01-25

    摘要: A process for producing liquid and, optionally, gaseous products from gaseous reactants comprises feeding gaseous reactants into a slurry bed of solid particles suspended in a liquid; allowing the reactants to react as they pass upwardly through the slurry bed, thereby to form liquid and, optionally, gaseous products; and separating liquid product from the solid particles by passing, in a filtration zone within the slurry bed, liquid product through a filtration medium in a first direction, so that a cake of the solid particles forms on the filtration medium. The passage of liquid product through the filtering medium is interrupted. The filtering medium is then backflushed by passing a flushing fluid through the filtering medium in a second direction, opposite to the first direction, for at least portions of the periods that the liquid product passage is interrupted, thereby to dislodge the cake from the filtering medium.

    摘要翻译: 用于从气态反应物生产液体和任选的气态产物的方法包括将气态反应物进料到悬浮在液体中的固体颗粒的淤浆床中; 允许反应物在它们向上通过浆料床时反应,从而形成液体和任选的气态产物; 并且通过在第一方向上通过过滤介质使液体产物在浆液床内的过滤区域内通过在过滤介质上形成固体颗粒的饼,从而将液体产物与固体颗粒分离。 液体产物通过过滤介质的通道被中断。 然后通过使冲洗流体在与第一方向相反的第二方向上通过冲洗流体至少部分液体产物通道被中断的时段内被冲洗,从而将滤饼从过滤介质中移出 。

    Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means
    8.
    再颁专利
    Hydrocarbon synthesis reactor employing vertical downcomer with gas disengaging means 有权
    采用具有气体分离装置的垂直降液管的烃合成反应器

    公开(公告)号:USRE37229E1

    公开(公告)日:2001-06-12

    申请号:US09133423

    申请日:1998-08-13

    IPC分类号: B01J808

    摘要: The operation of a hydrocarbon synthesis reactor and catalyst distributed in the reaction slurry therein are improved by the presence in said reactor of one or more vertical downcomers open at both ends with gas disengaging areas located at their top end. The downcomer which circulates catalyst from the top of the reaction slurry to the bottom of said slurry is fully immersed in the reaction slurry and preferably extends from just above the bottom of the reaction zone of the reaction vessel to just below the top surface of the reaction slurry. The bottom end of said downcomer is shielded from intrusion of rising synthesis gas by the placement of a baffle which blocks rising gas entry but facilitates the exit of catalyst and liquid from the bottom of said downcomer and distributes them radially throughout the adjacent reactor slurry.

    摘要翻译: 通过在位于其顶端的气体分离区域的两端开放的一个或多个垂直下降管的所述反应器中存在分布在其中的反应浆料中的烃合成反应器和催化剂的操作。 将催化剂从反应浆料的顶部循环到所述浆料的底部的降液管完全浸入反应浆料中,优选从反应容器的反应区的正上方延伸到反应的顶部表面正下方 泥浆。 所述降液管的底端通过放置阻挡上升气体进入的挡板而防止上升的合成气的入侵,但有利于催化剂和液体从所述降液管的底部排出并将其径向分布在相邻的反应器浆料中。