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用热力学相平衡理论和UNIFAC模型研究了渗透汽化从C6溶剂油中脱微量水的可行性,用自制的两种膜进行了渗透汽化脱水的小试和扩大试验,确定了适合该体系的脱水用膜和脱水工艺条件.

参考文献

[1] Lipnizki Frank;Ten Po-Kiong;Field Robert W. .Pervaporation-based hybrid process: A review of process design, applications and economics[J].Journal of Membrane Science,1999(2):183-210.
[2] 陈翠仙;余立新;祁喜旺 等.渗透汽化膜分离技术的进展及在石油化工中的应用[J].膜科学与技术,1997,17(03):14-18.
[3] Xianshe Feng;Robert Y.M.Huang .Liquid separation by membrane pervaporation: A review[J].Industrial & Engineering Chemistry Research,1997(4):1048-1066.
[4] Hansen H K;Rasmussen P;Fredenslund A et al.Vapor-liquid equilibria by UNIFAC group contribution.(5)Revision and extension[J].Industrial and Engineering Chemistry Research,1991,30:2352-2355.
[5] Gmehling J;Li Jiding;Schiller M .A modified UNIFAC model.(2) Present parameter matrix and results for different thermodynamic properties[J].Industrial and Engineering Chemistry Research,1993,32:178-193.
[6] Kojima K;Tochigi K.Prediction of vapor-liquid equilibria by the ASOG method[M].Tokyo:Kodansha-Elsevier,1979
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