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    • 6. 发明授权
    • Hydrolytic polymerization of epsilon-caprolactam
    • ε-己内酰胺的水解聚合
    • US4204049A
    • 1980-05-20
    • US11647
    • 1979-02-12
    • Paul MatthiesJoachim KundeWerner Hoerauf
    • Paul MatthiesJoachim KundeWerner Hoerauf
    • C08G69/16
    • C08G69/16
    • An improved process for the continuous polymerization of .epsilon.-caprolactam in the presence of water as initiator in a vertical downward-flow tubular reactor, in which the .epsilon.-caprolactam is partially polymerized at elevated temperature in a first, mechanically agitated reaction zone and is further polymerized in further reaction zones to the desired degree of polymerization. Poly-.epsilon.-caprolactam is discharged in the form of a melt. The polymerization is carried out at a gauge pressure of from 0.2 to 0.9 bar, constant in all reaction zones. The temperature in the first reaction zone is maintained according to the relationship t.ltoreq.265+43 p .degree.C., where p is the numerical value of the gauge pressure in bars which relationship is subject to the condition that the temperature be within the range of 260.degree. to 295.degree. C.
    • 在垂直向下流动的管式反应器中,在水作为引发剂存在下ε-己内酰胺的连续聚合的改进方法,其中ε-己内酰胺在第一机械搅拌的反应区中在升高的温度下部分聚合, 在进一步的反应区中聚合至所需的聚合度。 聚ε-己内酰胺以熔体的形式排出。 在0.2至0.9巴的表压下进行聚合,在所有反应区都是恒定的。 第一反应区中的温度根据t = 265 + 43 p℃的关系维持,其中p是以巴为单位的表压的数值,其关系受温度在 范围260〜295℃
    • 7. 发明授权
    • Continuous production of polycaprolactam having a regulated amino end
group content
    • 连续生产具有调节氨基末端基团的聚碳酸酯
    • US5149758A
    • 1992-09-22
    • US713303
    • 1991-06-11
    • Paul Matthies
    • Paul Matthies
    • C08G69/02C08G69/04C08G69/16
    • C08G69/16
    • Polycaprolactam having a regulated amino end group content is produced in a continuous process in which caprolactam is polymerized at 240.degree.-290.degree. C. in the presence of water as initiator and in the presence of a dicarboxylic acid as chain regulator by polymerizing caprolactam in a single stage in the presence of from 0.3 to 5% by weight of water and from 0.1 to 0.6% by weight of terephthalic acid and/or isophthalic acid, each percentage being based on caprolactam, at a uniform pressure through the entire polymerization time of from 1.0 to 1.9 bar, measured in the vapor phase above the polymerization zone, while maintaining a water content of from 0.1 to 0.5% by weight, until the sum total of the amino and carboxyl end group contents is from 115 to 150 meq/kg, with the proviso that the amino end group content does not drop below 25 meq/kg, measured on extracted polycaprolactam.
    • 具有调节氨基端基含量的聚己内酰胺在连续方法中制备,其中己内酰胺在水作为引发剂的存在下在240-290℃下聚合,并且在作为链调节剂的二羧酸存在下,通过在 在0.3至5重量%的水和0.1至0.6重量%的对苯二甲酸和/或间苯二甲酸的存在下,每个百分比基于己内酰胺,在均匀的压力下通过整个聚合时间从 1.0至1.9巴,在聚合区上方的汽相中测量,同时保持水含量为0.1至0.5重量%,直到氨基和羧基端基含量的总和为115至150毫当量/ 条件是在提取的聚己内酰胺上测定氨基端基含量不低于25meq / kg。