探讨了单体浓度、反应温度、引发剂用量等因素对聚合反应速率和产物特性黏数的影响。
The effects of monomer concentration, reaction temperature, initiator dosage on polymerization rate and intrinsic viscosity of product were investigated.
此外探讨了聚合反应条件对树脂吸油率和吸油速率的影响以及树脂的缓释性能。
The influences of reaction conditions on oil absorbency and swelling rate were studied, as well as slow release property.
以大豆油为原料，根据热聚合反应过程中黏度的变化确定反应的速率常数及热聚合反应的活化能。
The reaction rate constant and activation energy of soybean oil thermal polymerization reaction were determined by analysis of the change of viscosity.
转化率与粒径数据表明，随着乳化剂用量的增加，聚合反应速率和转化率均有所增加，粒径减小，这一趋势在反应初期表现得更为明显。
The kinetics of polymerization showed that the velocity and conversion of the polymerization increased while the particle size decreased as the amount of surfactant increased.
考察了热引发方式和不同种类、浓度下的引发剂引发方式在苯乙烯的本体聚合中对聚合反应速率和产品的分子量及其分子量分布的影响。
The effects of initiators and thermal initiation on a reaction rate, molecular weight and molecular weight distribution of products in a mass polymerization of styrene were investigated.
研究了影响XTBN的组成、分子量和微观结构，以及聚合反应速率的主要因素。
The essential factors which affect the composition, molecular weight, microstructure and the rate of polymerization of XTBN were studied.
重点介绍了聚合釜改造前后的聚合反应速率、键助剂的配方量及聚合工艺控制方面发生的重大变化。
Changes relating to the polymerization reaction rate, the key assistant agent formula ratio and the technological control are emphatically described.
实验结果表明，在聚合反应初期，聚合反应速率与引发剂的浓度呈半级反应，与单体浓度呈一级反应；
The results show that the reaction rate is in direct proportion to one power of monomer concentration and a half power of initiator concentration;
以大豆油为原料，根据热聚合反应过程中黏度的变化确定反应的速率常数及热聚合反应的活化能。
Taking soybean oil as raw material, the vehicle of soy ink was synthesized by heat polymerization under vacuum technology.
以大豆油为原料，根据热聚合反应过程中黏度的变化确定反应的速率常数及热聚合反应的活化能。
Taking soybean oil as raw material, the vehicle of soy ink was synthesized by heat polymerization under vacuum technology.
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