Process for production of ethylene oxide copolymer
    2.
    发明申请
    Process for production of ethylene oxide copolymer 审中-公开
    生产环氧乙烷共聚物的方法

    公开(公告)号:US20050197485A1

    公开(公告)日:2005-09-08

    申请号:US11051168

    申请日:2005-02-05

    摘要: An object of the present invention is to provide a process which can produce, easily and with good productivity and reproducibility, an ethylene oxide copolymer provided with desired compositional ratios of monomers and a desired molecular weight and further with a desired melting point. As a means of achieving this object, a process according to the present invention for production of an ethylene oxide copolymer is a process comprising a step of polymerizing a monomer mixture including ethylene oxide as a main component, thereby producing the ethylene oxide copolymer, with the process being characterized in that the polymerization step includes at least one step each of the following steps: a step in which only the ethylene oxide is supplied to thus polymerize it; and a step in which the ethylene oxide and another monomer are supplied to thus polymerize them.

    摘要翻译: 本发明的一个目的是提供一种可以制备具有期望组成比的单体和所需分子量并进一步具有所需熔点的环氧乙烷共聚物,能够容易地且具有良好的生产率和再现性的方法。 作为实现该目的的手段,根据本发明的环氧乙烷共聚物的制造方法是包括使包含环氧乙烷作为主要成分的单体混合物聚合的步骤,从而制备环氧乙烷共聚物, 方法的特征在于聚合步骤包括以下步骤中的至少一个步骤:仅供给环氧乙烷以使其聚合的步骤; 并且提供环氧乙烷和其它单体从而聚合它们的步骤。

    Process for producing polyester by ring-opening copolymerization
    4.
    发明授权
    Process for producing polyester by ring-opening copolymerization 失效
    通过开环共聚制备聚酯的方法

    公开(公告)号:US5391700A

    公开(公告)日:1995-02-21

    申请号:US233649

    申请日:1994-04-26

    IPC分类号: C08G63/42

    CPC分类号: C08G63/42

    摘要: This invention provides a process for producing with industrially good efficiency a polyester having a high melting point and biodegradability. In this process, ring-opening copolymerization of a cyclic acid anhydride containing succinic anhydride as a main component with a cyclic ether containing ethylene oxide as a main component is carried out in the presence of a catalyst by introducing successively the cyclic ether into a reaction vessel containing the cyclic acid anhydride in a melting state or solution state. The rate per hour of introducing the cyclic ether is within the range of 3 to 90 parts by weight per 100 parts by weight of the cyclic acid anhydride, and the reaction vessel has an inside pressure within the range of atmospheric pressure to 50 kgf/cm.sup.2 as a gauge pressure.

    摘要翻译: 本发明提供了具有高效率的具有高熔点和生物降解性的聚酯的工业生产方法。 在该方法中,以含有环氧乙烷为主要成分的环状醚作为主要成分的环状酸酐以环氧乙烷为主要成分的开环共聚在催化剂的存在下进行,连续将环状醚引入反应容器 含有处于熔融状态或溶液状态的环状酸酐。 环状醚的引入速度为每100重量份环状酸酐为3〜90重量份,反应容器的内部压力为大气压至50kgf / cm2 作为表压。