PROCESS FOR WORKING-UP A REACTION MIXTURE COMPRISING POLYETHER POLYOL
    41.
    发明申请
    PROCESS FOR WORKING-UP A REACTION MIXTURE COMPRISING POLYETHER POLYOL 有权
    用于加工包含聚醚多元醇的反应混合物的方法

    公开(公告)号:US20130146537A1

    公开(公告)日:2013-06-13

    申请号:US13712536

    申请日:2012-12-12

    IPC分类号: B01D61/24

    摘要: The invention relates to a process for working-up a reaction mixture (5) comprising polyetherol and dissolved alkali metal comprising catalyst, wherein at least alkali metal ions of the dissolved alkali metal comprising catalyst are partially or completely removed from the mixture by a membrane separation process, the process comprising following steps: (a) feeding the reaction mixture (5) comprising polyetherol and dissolved alkali metal comprising catalyst into a first chamber (1) of a separation unit (3), (b) feeding a solvent into a second chamber (7) of the separation unit (3), the first chamber (1) and the second chamber (7) being separated by a membrane (9), (c) transporting at least the alkali metal ions of the alkali metal comprising catalyst from the first chamber (1) into the second chamber by passing through the membrane (9).

    摘要翻译: 本发明涉及一种用于处理包含聚醚醚和包含催化剂的溶解的碱金属的反应混合物(5)的方法,其中至少包含催化剂的溶解的碱金属的碱金属离子通过膜分离部分或完全从混合物中除去 方法包括以下步骤:(a)将包含聚乙烯醇和包含催化剂的溶解的碱金属的反应混合物(5)进料到分离单元(3)的第一室(1)中,(b)将溶剂进料到第二 分离单元(3)的室(7),第一室(1)和第二室(7)被隔膜(9)隔开,(c)至少输送包含催化剂的碱金属的碱金属离子 从第一腔室(1)通过膜(9)进入第二腔室。

    PROCESS FOR CONTINUOUS HYDROGENATION OR HYDROGENATING AMINATION
    42.
    发明申请
    PROCESS FOR CONTINUOUS HYDROGENATION OR HYDROGENATING AMINATION 失效
    连续加氢或加氢胺化的方法

    公开(公告)号:US20120232267A1

    公开(公告)日:2012-09-13

    申请号:US13423956

    申请日:2012-03-19

    IPC分类号: C07D265/30 C07C45/62

    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。