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    • 1. 发明授权
    • Continuous preparation of low unsaturation polyoxyalkylene polyether
polyols with continuous additon of starter
    • 连续添加起始剂连续制备低不饱和聚氧化烯聚醚多元醇
    • US5689012A
    • 1997-11-18
    • US683356
    • 1996-07-18
    • Jose F. PazosT. Thomas Shih
    • Jose F. PazosT. Thomas Shih
    • C08G65/10C08G65/26C07C43/11
    • C08G65/2663C08G65/2696
    • A continuous process for the preparation of polyoxyalkylene polyethers using DMC catalysts as the polyoxyalkylation catalyst employs continuous addition of alkylene oxide in conjunction with continuous addition of starter and catalyst to a continuous oxyalkylation reactor. Despite the continuous introduction of starter, the molecular weight distribution of the polyether product is quite narrow, as indicated by the exceptionally low polydispersity of the product. The presence of low molecular weight species during the majority of the polyoxyalkylation also substantially eliminates extremely high molecular weight fractions having molecular weights greater than 100,000 Da, again without appreciably broadening molecular weight distribution. By withdrawing intermediate molecular weight polyether product or diverting a portion of the end product to prepare a catalyst/starter mixture, rapid and sustained reaction rates can be achieved while employing low molecular weight starters. Continuous build ratios in excess of 0.98 can be achieved.
    • 使用DMC催化剂作为聚氧化烷基化催化剂制备聚氧化烯聚醚的连续方法是连续加入环氧烷,连续加入引发剂和催化剂至连续的烷氧基化反应器。 尽管连续引入起始物,但聚醚产物的分子量分布相当窄,如产物的多分散性极差。 在大部分聚氧化烷基化期间低分子量物质的存在也基本上消除了分子量大于100,000Da的极高分子量级分,同时又没有明显地扩大分子量分布。 通过取出中间分子量聚醚产物或转移一部分最终产物以制备催化剂/起始混合物,可以在使用低分子量起始剂的同时实现快速和持续的反应速率。 连续建造率可以达到0.98以上。