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    • 9. 发明授权
    • Continuous process for the production of polyether polyols
    • 连续生产聚醚多元醇的方法
    • US06410801B1
    • 2002-06-25
    • US09442882
    • 1999-11-18
    • Werner HinzEdward Michael Dexheimer
    • Werner HinzEdward Michael Dexheimer
    • C07C4320
    • C08G59/3209B01J19/242B01J19/243B01J2219/0002B01J2219/00033B01J2219/00094C08G65/2696
    • A continuous alkoxylation process for the production of polyether polyols is disclosed. The process comprises the use of a plurality of reaction modules each having an outer tube and an inner tube with annular chamber between them. A spiral reaction tube is spaced from the inner tube and winds around the inner tube within the annular chamber. The spiral reaction tube includes an inlet and an outlet, each of which extend through said outer tube. A heat exchange medium flows through the annular chamber and controls the reaction temperature in the spiral reaction tube. The process comprises continuously forming an initial reaction mixture of at least one alkylene oxide and an initiator having at least one reactive hydrogen which is reactive to the alkylene oxide. Continuously flowing the initial reaction mixture through a first spiral reaction tube having an internal diameter and a spiral diameter that promote a pseudo-turbulent flow of the initial reaction mixture through the first spiral reaction tube to form a reaction product. Then flowing the reaction product into a second spiral reaction tube and adding a catalyst and an alkylene oxide to the reaction product, the second spiral reaction tube having an internal diameter and a spiral diameter that promote a pseudo-turbulent flow of the reaction product, the catalyst and the alkylene oxide in the second spiral reaction tube.
    • 公开了用于生产聚醚多元醇的连续烷氧基化方法。 该方法包括使用多个反应模块,每个反应模块具有外管和在它们之间具有环形室的内管。 螺旋反应管与内管间隔开并围绕环形室内的内管缠绕。 螺旋反应管包括入口和出口,每个入口和出口延伸穿过所述外管。 热交换介质流过环形室,并控制螺旋反应管中的反应温度。 该方法包括连续地形成至少一种环氧烷和具有至少一个与环氧烷反应的反应性氢的引发剂的初始反应混合物。 将初始反应混合物连续流过具有内径和螺旋直径的第一螺旋反应管,该第一螺旋反应管促使初始反应混合物通过第一螺旋反应管的假湍流,形成反应产物。 然后将反应产物流入第二螺旋反应管并向反应产物中加入催化剂和烯化氧,第二螺旋反应管具有促进反应产物的假湍流的内径和螺旋直径, 催化剂和第二螺旋反应管中的环氧烷。