依据相平衡理论,有机溶剂在聚合物膜中达到溶解平衡时,组分i在液相中化学势应等于其在聚合物膜相中的化学势.文中用UNIQUAC活度系数模型计算组分在液相中的活度,UNIFAC+FV基团贡献法关联有机溶剂在聚合物膜中的活度,理论预测了聚丙烯(PP)膜在正戊烷和正己烷中的溶胀行为.与文献实测值进行比较,一定程度上二者能够吻合.若考虑聚合物膜粘弹性的影响,计算结果有所改进.鉴于UNIFAC+FV法无需组分间交互作用参数,值得推荐.
参考文献
[1] | Lee B C;Danner R P .[J].AICHE Journal,42(03):837-849. |
[2] | Meien O F;Biscaia E C;Nobrega R.[J].AICHE Journal(11):2932-2942. |
[3] | Abrams D S;Prausnitz J M.[J].AICHE Journal:116-128. |
[4] | Fredenslund A;Jones R L;Prausnitz J M.[J].AICHE Journal:1086-1099. |
[5] | Magnussen T;Rasmussen P;Frenendlund A.[J].Industrial & Engineering Chemistry Process Design and Development:331-339. |
[6] | Gmehling J;Anderson T F;Prausnitz J M.[J].Industrial and Engineering Chemistry Research:269-273. |
[7] | Tochigi K;Tiegs D;Gmehling J.[J].Journal of Chemical Engineering of Japan,1990(04):453-463. |
[8] | 潘勤敏;顾培韵.[J].合成橡胶工业,1991(04):198-307. |
[9] | Elbro H S;Fredenslund A;Rasmussen P A.[J].Macromolecules:4707-4714. |
[10] | Bondi A.[J].Journal of Physical Chemistry:441-451. |
[11] | Holten A J;Fredenslund A;Rasmussen P.[J].Industrial and Engineering Chemistry Research:1382-1390. |
[12] | Chen F;Fredenslund A;Rasmussen P.[J].Industrial and Engineering Chemistry Research:875-882. |
[13] | Oishi T;Prausnitz J M.[J].Industrial & Engineering Chemistry Process Design and Development:333. |
[14] | Castro E F;Gonzo E E;Gottifredi J C.[J].Journal of Membrane Science,1996:57-64. |
[15] | 魏文德.有机化工原料大全[M].北京:化学工业出版社,1994:221-223. |
[16] | Prausnitz J M.Englewood Cliffs[M].N.J.:Prentice-Hall,1980 |
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