Process for continuous hydrogenation or hydrogenating amination
    3.
    发明授权
    Process for continuous hydrogenation or hydrogenating amination 失效
    连续氢化或氢化胺化的方法

    公开(公告)号:US08557985B2

    公开(公告)日:2013-10-15

    申请号:US13423956

    申请日:2012-03-19

    摘要: A process continuously hydrogenating unsaturated compounds, in which particles of a first hydrogenation catalyst are suspended in a liquid phase in which an unsaturated compound is dissolved, the liquid phase, in the presence of a hydrogenous gas at a first partial hydrogen pressure and at a first temperature, is conducted through a packed bubble column reactor in cocurrent counter to the direction of gravity, the effluent from the bubble column reactor is sent to a gas-liquid separation, the liquid phase is sent to a crossfiltration to obtain a retentate and a filtrate, the retentate is recycled into the bubble column reactor and the filtrate, in the presence of a hydrogenous gas at a second partial hydrogen pressure and at a second temperature, is passed over a bed of a second hydrogenation catalyst, the second partial hydrogen pressure is at least 10 bar higher than the first partial hydrogen pressure.

    摘要翻译: 将第一氢化催化剂的颗粒悬浮在其中溶解有不饱和化合物的液相中的不饱和化合物的液相,在第一部分氢气压力下的氢气存在下的液相, 温度,通过与泡沫塔反应器并流反向并流并通过气泡塔反应器进行气液分离,将液相送至交叉过滤以获得滞留物和滤液 ,将渗余物再循环到泡罩塔反应器中,并且在第二部分氢气压力和第二温度下在氢气存在下将滤液通过第二氢化催化剂床,第二部分氢气压力为 比第一部分氢气压力高至少10巴。

    Process for continuous hydrogenation or hydrogenating amination
    10.
    发明授权
    Process for continuous hydrogenation or hydrogenating amination 有权
    连续氢化或氢化胺化的方法

    公开(公告)号:US08163963B2

    公开(公告)日:2012-04-24

    申请号:US12090377

    申请日:2006-10-16

    IPC分类号: C07C45/00

    摘要: A process is described for continuously hydrogenating unsaturated compounds, in which particles of a first hydrogenation catalyst are suspended in a liquid phase in which an unsaturated compound is dissolved, the liquid phase, in the presence of a hydrogenous gas at a first partial hydrogen pressure and at a first temperature, is conducted through a packed bubble column reactor in cocurrent counter to the direction of gravity, the effluent from the bubble column reactor is sent to a gas-liquid separation, the liquid phase is sent to a crossfiltration to obtain a retentate and a filtrate, the retentate is recycled into the bubble column reactor and the filtrate, in the presence of a hydrogenous gas at a second partial hydrogen pressure and at a second temperature, is passed over a bed of a second hydrogenation catalyst, wherein the second partial hydrogen pressure is at least 10 bar higher than the first partial hydrogen pressure.

    摘要翻译: 描述了在第一部分氢气压力下在氢气存在下将不饱和化合物连续氢化的方法,其中第一氢化催化剂的颗粒悬浮在其中溶解不饱和化合物的液相中,液相,以及 在第一个温度下,通过气泡塔反应器与重力方向并流,将来自泡罩塔反应器的流出物送入气液分离,将液相送至交叉过滤,得到滞留物 和滤液,将滞留物再循环到泡罩塔反应器中,并且在第二部分氢气压力和第二温度下在氢气存在下将滤液通过第二氢化催化剂床,其中第二 部分氢气压力比第一部分氢气压力高至少10巴。