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The suspension copolymerisation of isobutylene with isoprene in a tubular turbulent reactor: the kinetics of the chemical process and the mass and heat transfer

机译:异丁烯与异戊二烯在管式湍流反应器中的悬浮共聚:化学过程的动力学以及传质和传热

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摘要

The macrokinetics of the synthesis of butyl rubber (cationic copolymerisation of isobutylene with isoprene over an AIC3 catalyst in a CH3Cl medium, initial synthesis temperature 173 K) in a circular-type tubular turbulent reactor was calculated. It was established that, with decrease in the size of the reaction region (cylinder diameter reduced from 0.2 to 0.1 m) and in the flow rate of the reaction suspension (reduced from 10 to 1 m/s), there is a reduction in the number-average molecular weight (from 91 700 to 1360) and in the weight-average molecular weight (from 257 000 to 134 000) of the synthesised butyl rubber and an increase in its polydispersity (from 2.8 to 110).
机译:计算了在圆形管式湍流反应器中丁基橡胶合成的宏观动力学(异丁烯与异戊二烯在AIC3催化剂上在CH3Cl介质中进行阳离子共聚,初始合成温度为173 K)。已经确定,随着反应区域尺寸的减小(圆筒直径从0.2 m减小至0.1 m)和反应悬浮液的流速(从10 m / s减小至1 m / s),减小了合成丁基橡胶的数均分子量(从91700到1360)和重均分子量(从257 000到134 000)以及其多分散性增加(从2.8到110)。

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