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    • 103. 发明授权
    • Method of regulating molecular weight distribution of polyether glycol
    • 调节聚醚二醇分子量分布的方法
    • US06395938B1
    • 2002-05-28
    • US09701007
    • 2000-11-22
    • Takaharu Akedo
    • Takaharu Akedo
    • C07C4101
    • C08G65/2696C08G65/20C08G65/2666
    • A method for controlling the molecular weight distribution of polyether glycol in producing polyether glycol having a specified number average molecular weight by polymerizing tetrahydrofuran as a starting monomer with the use of a heteropoly-acid as a catalyst, which method comprises conducting the polymerization in the presence of an amount of water which can form two phases of the organic phase and a catalyst phase, sampling the polymerization product during the polymerization to determine the molecular weight distribution and, when the molecular weight distribution thus found is narrower than the specified molecular weight distribution, making the residence time distribution of the starting monomer in the catalyst phase wider, while, when the found molecular weight distribution is wider than the specified molecular weight distribution, making the residence time distribution of the starting monomer in the catalyst phase narrower.
    • 通过使用杂多酸作为催化剂聚合四氢呋喃作为起始单体来控制聚醚二醇在制备具有特定数均分子量的聚醚二醇中的分子量分布的方法,该方法包括在存在下进行聚合 的一定量的水可以形成有机相和催化剂相的两相,在聚合期间对聚合产物进行取样以确定分子量分布,并且当所发现的分子量分布窄于指定的分子量分布时, 使得起始单体在催化剂相中的停留时间分布更宽,而当发现的分子量分布大于特定的分子量分布时,使起始单体在催化剂相中的停留时间分布变窄。
    • 110. 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。