This article introduces some new constructions of inside cold parts for polymerization reactor of synthesis rubber latex.
本文主要介绍了在胶乳聚合釜内冷装置设计中采用的一些新型结构以及计算方法。
The hardware and software configuration of CS3000, the temperature control mode of polymerization reactor and the condenser were introduced.
简述了CS3000系统白勺硬件构造和软件组态，介绍了聚合釜和冷凝器白勺温度控制程序。
The hardware and software configuration of CS3000 , the temperature control mode of polymerization reactor and the condenser were introduced.
简述了CS3000系统的硬件结构和软件组态，介绍了聚合釜和冷凝器的温度控制程序。
This controller has been used in a computer control system for the semi-batch processing polymerization reactor at Zhong-Shan Chemical Factory of Nanjing.
该控制器在南京钟山化工厂半间歇式聚合釜生产过程的计算机控制系统中得到了实际应用。
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.
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。
Pectic oligosaccharide produced by microwave and autoclave extraction were observed with higher degrees of polymerization than those by an ultrafiltration membrane enzyme reactor.
用微波和高压提取的方法提取的果胶低聚糖比用超滤膜酶反应器的提取的具有更高的聚合度。
During ionic polymerization and group transfer polymerization, the absolute need to be transferred to the reactor anhydrous reagents.
在进行离子型聚合和基团转移聚合时，需要将绝对无水试剂转移到反应装置。
The polymerization conditions of ammonium polyphosphate(APP) were studied by microwave reactor and muffle furnace respectively with ammonium dihydrogen phosphate and urea as raw materials.
以磷酸二氢铵和尿素为原料，用微波反应器和马弗炉分别研究聚磷酸铵（APP）的聚合工艺条件。
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。
In a tower reactor polymerization may be carried out in two zones.
塔式反应器中聚合可分为两段进行。
The liquid phase bulk propylene polymerization in loop reactor was simulated based on the polymerization mechanism.
采用机理建模方法，研究了丙烯在环管反应器中的液相本体聚合过程。
The balance between the maximum reaction rate and the heat transfer capacity of the reactor was the key factor for shortening of polymerization time and improving the production capacity.
最大聚合速率与聚合釜传热能力的均衡是达到缩短聚合时间、提高生产能力的重要环节。
At present, the polymerization of polymer is largely by batch chemical reactor, account for 90%.
目前聚合物生产中的聚合反应主要是在间歇式反应釜中进行，约占总聚合装置的90%。
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.
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。
The liquid phase bulk propylene polymerization in loop reactor was simulated based on the propylene polymerization mechanism.
本文对结构和受载都非常复杂的聚丙烯环管反应器建立了有限元分析设计模型。
The liquid phase bulk propylene polymerization in loop reactor was simulated based on the propylene polymerization mechanism.
本文对结构和受载都非常复杂的聚丙烯环管反应器建立了有限元分析设计模型。
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