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Process for preparation of spinnable solutions of acrylonitrile polymers or copolymers having a high-acrylonitrile content

机译:制备具有高丙烯腈含量的丙烯腈聚合物或共聚物的可纺溶液的方法

摘要

Spinnable solutions of polyacrylonitrile, or of copolymers containing over 85% by weight of acrylonitrile, are produced by polymerization of the monomer(s) in dimethyl formamide in at least two sequential stages, in the first of which the polymerization is carried out at 60 DEG to 65 DEG C. until reaching not less than 30% and not more than 40% conversion of the monomer(s), while in the second stage or the following stages the polymerization is carried on under controlled temperature conditions until reaching a higher conversion, the amount of dimethyl formamide and catalyst required to attain said higher conversion being divided into as many fractions as there are stages and one of said fractions being individually added at the beginning of each stage. The final conversion attained is desirably in the range 70 to 80%. The temperature conditions may be controlled by carrying out the process under sub-atmospheric pressure, in which case the polymerization is terminated by increasing the pressure and distilling off unreacted monomer(s). In the examples, the polymerization is carried out in two stages. In Examples 1 and 3 copolymers of acrylonitrile, sodium allyl sulphonate and methyl methacrylate are prepared and in Example 2 a copolymer of acrylonitrile, sodium allyl sulphonate and ethyl acrylate. Lauroyl peroxide is used as catalyst and thiourea dioxide is present in the reaction solutions of Examples 1 and 2.
机译:通过使单体在二甲基甲酰胺中的至少两个连续阶段的聚合反应来生产聚丙烯腈或含有大于85重量%的丙烯腈的共聚物的可纺溶液。至65℃直至单体的转化率不小于30%且不大于40%,而在第二阶段或随后的阶段中,聚合在受控的温度条件下进行直至达到较高的转化率,将达到所述较高转化率所需的二甲基甲酰胺和催化剂的量分成与阶段一样多的馏分,并且在每个阶段的开始分别添加所述馏分之一。期望的最终转化率在70-80%的范围内。温度条件可通过在低于大气压的压力下进行的方法来控制,在这种情况下,通过增加压力并蒸馏出未反应的单体来终止聚合反应。在实施例中,聚合反应分两个阶段进行。在实施例1和3中,制备了丙烯腈,烯丙基磺酸钠和甲基丙烯酸甲酯的共聚物,在实施例2中,制备了丙烯腈,烯丙基磺酸钠和丙烯酸乙酯的共聚物。过氧化月桂酰用作催化剂,实施例1和2的反应溶液中存在二氧化硫脲。

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