The emulsion copolymerization of acrylates(methylmethacrylate,bulylacrylate acry lic acid,hydroxyethylmethacrylate) and vinyltriethoxysilane(VTS) using a reactive emulsifier DNS-86 has been studied as function of emul...The emulsion copolymerization of acrylates(methylmethacrylate,bulylacrylate acry lic acid,hydroxyethylmethacrylate) and vinyltriethoxysilane(VTS) using a reactive emulsifier DNS-86 has been studied as function of emulsifier a mount, initiator amount, VTS amount, HEMA amount and polymerization temperature. The results showed that the monomer conversion i ncreased with increase in emulsifier amount, initiator amount , amount of HEMA monomer and reaction temperature, but decreased w ith increase in the amount of VTS monomer.展开更多
研究了在反应性乳化剂SE-10N存在下,采用半连续滴加工艺进行苯丙乳液共聚合的表观动力学。首先利用间歇法研究了引发剂、乳化剂用量、单体总量和温度对聚合反应速率的影响,得到了相应的聚合反应速率方程为Rp=k[M]0.30[I]0.18[E]0.97,并...研究了在反应性乳化剂SE-10N存在下,采用半连续滴加工艺进行苯丙乳液共聚合的表观动力学。首先利用间歇法研究了引发剂、乳化剂用量、单体总量和温度对聚合反应速率的影响,得到了相应的聚合反应速率方程为Rp=k[M]0.30[I]0.18[E]0.97,并计算得到聚合反应的表观活化能为90.8 kJ.m o-l1。然后采用半连续滴加法,讨论了不同滴加速率对聚合表观速率Rp的影响,结果表明,随滴加速率Ra的增加,反应速率Rp也增加,但增加的幅度逐渐减少,且聚合过程的状态不断远离饥饿态。要使该聚合过程的状态保持在稳定的饥饿态,单体滴加时间应控制在140 m in以上。展开更多
文摘The emulsion copolymerization of acrylates(methylmethacrylate,bulylacrylate acry lic acid,hydroxyethylmethacrylate) and vinyltriethoxysilane(VTS) using a reactive emulsifier DNS-86 has been studied as function of emulsifier a mount, initiator amount, VTS amount, HEMA amount and polymerization temperature. The results showed that the monomer conversion i ncreased with increase in emulsifier amount, initiator amount , amount of HEMA monomer and reaction temperature, but decreased w ith increase in the amount of VTS monomer.
文摘研究了在反应性乳化剂SE-10N存在下,采用半连续滴加工艺进行苯丙乳液共聚合的表观动力学。首先利用间歇法研究了引发剂、乳化剂用量、单体总量和温度对聚合反应速率的影响,得到了相应的聚合反应速率方程为Rp=k[M]0.30[I]0.18[E]0.97,并计算得到聚合反应的表观活化能为90.8 kJ.m o-l1。然后采用半连续滴加法,讨论了不同滴加速率对聚合表观速率Rp的影响,结果表明,随滴加速率Ra的增加,反应速率Rp也增加,但增加的幅度逐渐减少,且聚合过程的状态不断远离饥饿态。要使该聚合过程的状态保持在稳定的饥饿态,单体滴加时间应控制在140 m in以上。