从设备与工艺两方面剖析了PA6生产前聚合反应器的设计。
The design of PA6 prepolymerization reactor was discussed from the aspects of equipment and technological process.
综述了聚合反应器的防粘釜和清釜技术，并简介在悬浮聚合反应器中的应用。
The techneques of scale prevention and cleaning of polymerization reactors, and their application to the suspension polymerization reactors were reviewed with 22 references.
所述混合物在加入至少一种交联剂与进入聚合反应器之间的停留时间为小于180秒。
The retention time of the mixture between addition of the at least one cross-linking agent and entry into the polymerization reactor is less than 180 seconds.
讨论了间歇式和连续式溶液聚合反应器的特点，并相应推荐了一些新型溶液聚合反应器。
The features of batch and continuous solution polymerization reactors were discussed and some new solution polymerization reactors were recommended with 7 references.
应用电子计算机对两种理想流动模型的苯乙烯本体热聚合反应器进行了初步数学模拟试验。
Mathematical simulation has been performed by means of electronic computor for two types of ideal flow reactor systems used for the thermal bulk polymerization of styrene.
通过对LLDPE聚合反应器表观气速(sgv)值的计算，为流化参数的控制提供了理论依据。
This paper elucidated the theoretical basis for controlling the fluidization parameters by calculating the SGV surface gas velocity in he LLDPE reactor.
该反应器较好的解决了本体聚合反应中的传热，高粘性物料的出料和固体产物的出料等问题。
That reactor resolved the problem of transfering heat, taking out highly viscous material and solid outcome in bulk polymerization.
该反应器较好的解决了本体聚合反应中的传热，高粘性物料的出料和固体产物的出料等问题。
That reactor resolved the problem of transfering heat, taking out highly viscous material and solid outcome in bulk polymerization.
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