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    吴君毅, 张冰冰, 周兴贵. 卧式反应釜中的偏氟乙烯(VDF)分散聚合动力学[J]. 华东理工大学学报(自然科学版), 2012, (4): 408-415.
    引用本文: 吴君毅, 张冰冰, 周兴贵. 卧式反应釜中的偏氟乙烯(VDF)分散聚合动力学[J]. 华东理工大学学报(自然科学版), 2012, (4): 408-415.
    WU Jun-yi, ZHANG Bing-bing2,, ZHOU Xing-gui. Dispersion Polymerization Kinetics of Vinylidene Fluoride in a Horizontal Reactor[J]. Journal of East China University of Science and Technology, 2012, (4): 408-415.
    Citation: WU Jun-yi, ZHANG Bing-bing2,, ZHOU Xing-gui. Dispersion Polymerization Kinetics of Vinylidene Fluoride in a Horizontal Reactor[J]. Journal of East China University of Science and Technology, 2012, (4): 408-415.

    卧式反应釜中的偏氟乙烯(VDF)分散聚合动力学

    Dispersion Polymerization Kinetics of Vinylidene Fluoride in a Horizontal Reactor

    • 摘要: 以分散聚合中的低聚物机理以及自由基聚合相关理论为基础得到了偏氟乙烯分散聚合的动力学模型,进而在卧式反应釜中研究了反应温度50 ℃下偏氟乙烯分散聚合过程中引发剂质量浓度(ρI)、单体质量浓度(ρM)、乳化剂质量浓度(ρS)对反应速率(Rp)和单位体积乳胶粒数(Np)的影响,其中Np=1.01×1019ρ1.92Sρ0.10I,0ρ-3.11M,0,以及Rp=1.76×10-8 Φ1/3ρ 0.36Sρ 0.60Iρ3.83M。根据VDF分散聚合模型可进一步对Rp关系式进行分解,并与模型式对比后可以发现Rp与Np呈0.19级关系,接近于模型中的1/6级。此外,由模型式中的K0定义以及相关参数值可以得到在该反应条件下单体在水相和反应区的分配系数(α)为1.50×10-4。

       

      Abstract: The polymerization kinetics model of vinylidene difluoride was deduced based on the oligomer mechanism of dispersion polymerization and the theories of free radical polymerization in this paper. The relationships of reaction rate (Rp) and particle number per unit volume (Np) with initiator concentration (ρI), monomer concentration (ρM) and emulsifier concentration (ρS) in a horizontal reactor were studied. Under the reaction conditions, Np=1.01×1019ρ1.92Sρ0.10I,0ρ-3.11M,0 and Rp=1.76×10-8×Φ1/3ρ 0.36Sρ 0.60Iρ 3.83M were acquired. Compared to VDF dispersion polymerization model, the equation of Rp can be further rearranged and the effect of Np on Rp is the exponent of 0.19, similar to the model value of 1/6. According to the definition of K0 and the parameter values from literature, partition coefficient (α), which is the ratio of VDF monomer in the water phase and in the reaction area, is 1.50×10-4 by calculation.

       

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