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    • 1. 发明授权
    • Method and apparatus for controlling polybutene production
    • 控制聚丁烯生产的方法和装置
    • US4620049A
    • 1986-10-28
    • US666896
    • 1984-10-31
    • Gregory E. SchmidtLinus K. LeungLawrence J. BeckDavid S. Chang
    • Gregory E. SchmidtLinus K. LeungLawrence J. BeckDavid S. Chang
    • C07C2/06C08F10/08C07C2/00
    • C07C2/06C08F10/08C08F2400/02Y10S208/01
    • The method is particularly adapted for controlling the molecular weight of a product output from a polybutene reactor. The method includes the steps of: deriving from the operating parameter of a polybutene reactor system a formula which correlates molecular weight as determined by product viscosity or other parameters of the product output with operating variables such as temperature of the reactor and concentration of isobutylene in the reactor, which concentration can be controlled by the amount of catalyst, e.g., aluminum chloride, being fed into the reactor; monitoring (a) the temperature of the reactor, (b) the concentration of isobutylene in the reactor, (c) the flow of coolant supplied to the reactor for controlling the temperature thereof and (d) the feed rate of catalyst into the reactor; calculating with said algorithm the approximate molecular weight of the product output; determining if the desired product molecular weight is higher or lower than the calculated molecular weight; and, if higher or lower, altering, through use of the formula, the temperature and/or the concentration of isobutylene in the reactor to obtain the desired product molecular weight.Also the method can include the step of adding moisture to the feed or the reactor for lowering the molecular weight of the polybutene product output.The apparatus includes a reactor, a computer and various sensing, monitoring and control devices for carrying out the steps of the method.
    • 该方法特别适于控制从聚丁烯反应器输出的产物的分子量。 该方法包括以下步骤:从聚丁烯反应器系统的操作参数得出将通过​​产物粘度或其他产物输出参数确定的分子量与反应器温度和异丁烯浓度等操作变量相关联的公式, 反应器,该浓度可以通过进料到反应器中的催化剂的量例如氯化铝来控制; 监测(a)反应器的温度,(b)反应器中异丁烯的浓度,(c)供应给反应器的冷却剂流量用于控制其温度,和(d)催化剂进入反应器的进料速率; 用所述算法计算产品输出的近似分子量; 确定所需产物分子量是否高于或低于计算的分子量; 并且如果更高或更低,通过使用公式改变反应器中的异丁烯的温度和/或浓度以获得所需的产物分子量。 该方法还可以包括向进料或反应器中加入水分以降低聚丁烯产物的分子量的步骤。 该装置包括反应器,计算机以及用于执行该方法的步骤的各种感测,监视和控制装置。