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    • 5. 发明授权
    • Process for preparing polyacetal copolymer
    • 制备聚缩醛共聚物的方法
    • US5844059A
    • 1998-12-01
    • US791469
    • 1997-01-27
    • Kaoru YamamotoHiroyuki Kanai
    • Kaoru YamamotoHiroyuki Kanai
    • C08G2/06C08G2/10C08G2/18C08G2/28C08G6/00C08G2/00
    • C08G2/18C08G2/06C08G2/10C08G2/28
    • To prepare a thermally very stable polyacetal copolymer containing a very small amount of unstable parts in a high yield according to a simple process wherein an isopolyacid or an acid salt thereof is used as the polymerization catalyst in the copolymerization of trioxane as the principal monomer with a comonomer copolymerizable therewith, and wherein deactivation of the catalyst can be effected simply without fail through contact with a basic gas after polymerization without the necessity for any washing step. In the preparation of a polyacetal copolymer by the copolymerization of trioxane as the principal monomer with a cyclic ether or cyclic formal having at least one carbon--carbon bond as a comonomer, the copolymerization is effected using an isopolyacid or an acid salt thereof as the polymerization catalyst, followed by contact with a basic gas as a deactivator to deactivate the catalyst, and subsequent heat-melting treatment of the resulting crude polymer intact without washing thereof.
    • 为了制备含有非常少量的不稳定部分的热非常稳定的聚缩醛共聚物,根据简单的方法,其中在三恶烷作为主要单体的共聚合中使用异多酸或其酸盐作为聚合催化剂, 可与其共聚的共聚单体,并且其中催化剂的失活可以通过在聚合后与碱性气体接触而简单地进行,而不需要任何洗涤步骤。 在通过三恶烷作为主要单体与具有至少一个碳 - 碳键作为共聚单体的环状醚或环状缩甲醛进行共聚制备聚缩醛共聚物时,使用等多酸或其酸性盐作为聚合反应进行共聚 催化剂,然后与作为失活剂的碱性气体接触以使催化剂失活,随后对所得粗聚合物进行热熔融处理而不洗涤。
    • 7. 发明授权
    • Method of continuous manufacturing of polymers or copolymers of trioxane
    • 连续制造三恶烷的聚合物或共聚物的方法
    • US4727132A
    • 1988-02-23
    • US861031
    • 1986-05-08
    • Tsuyoshi MinamisawaShuichi ChinoNoboru GotoMasaaki Nakamura
    • Tsuyoshi MinamisawaShuichi ChinoNoboru GotoMasaaki Nakamura
    • B01J19/20C08G2/00C08G2/10C08G2/18
    • C08G2/10B01J19/20C08G2/18
    • A trioxane polymer is continuously produced with a continuous stirring-mixing apparatus. The apparatus includes two mutually parallel rotational shafts, a large number of paddles mounted on each rotational shaft and a barrel having an inside wall surface along the circular surface traced by the respective paddles, as they rotate. Thus, the barrel has a cross-section in the shape of two circles concentric with the two rotational shafts, which overlap each other. The apparatus is also provided with a temperature controlling jacket. In the operation of the apparatus, a material mixture of trioxane, catalyzer, other copolymerizable comonomers, as the case may be, and additives, is continuously fed in through a material supply port located at one end thereof, then, the material mixture is subjected to polymerization or copolymerization reaction, while being stirred by turning the aforementioned rotational shafts in an opposite direction to each other and, thereafter, the polymers or copolymers of trioxane are taken out as fine granules through a discharge port located at the other end thereof. The method is characterized in that at least one set of paddles of a sectional shape which meets a requirement that when a pair of paddles facing each other are turned in different directions around their rotational axes, the clearance between them shall be kept always as narrow as less than 3/100 of the barrel ID, are mounted on each shaft, adjoining each other, and the different direction turning is made in a state such that the clearance between the farthest part from the rotational axis of said paddle and the inside wall of the barrel are always maintained as narrow as less than 3/100 of the barrel ID.
    • 用连续搅拌混合装置连续生产三恶烷聚合物。 该装置包括两个相互平行的旋转轴,安装在每个旋转轴上的大量叶片和当旋转时由相应叶片沿着圆形表面的内壁表面的筒体。 因此,筒体具有与两个相互重叠的两个旋转轴同心的两个圆形的横截面。 该设备还设置有温度控制护套。 在设备的操作中,三恶烷,催化剂,其他可共聚的共聚单体的材料混合物(视情况而定)和添加剂通过位于其一端的材料供给口连续进料,然后将材料混合物 进行聚合或共聚反应,同时通过将上述旋转轴彼此相反的方向转动而进行搅拌,此后,通过位于其另一端的排出口将三恶烷的聚合物或共聚物作为细颗粒取出。 该方法的特征在于,至少一组截面形状的桨叶满足要求当一对彼此相对的桨叶围绕其旋转轴线在不同方向转动时,它们之间的间隙应保持总是如 小于3/100的桶ID,安装在彼此相邻的每个轴上,并且不同的方向转动形成为使得最远部分与所述桨叶的旋转轴线之间的间隙和 枪管始终保持在小于桶ID的3/100以下的窄度。