摘要
Ionic liquids have received increasing attention for their potential uses as non-wolatile separation and reaction solvents, and the liquid-liquid equilibrium(LLE)of ionic liquid containing systems is of great importance for such practical applications.The NRTL(non-random two liquid)equation was extended and used in this paper for the calculation of the LLE data of some ionic liquid-alcohol binary systems.It was found that the extended NRTL model could be accurately used to represent the LLE of these ionic liquid-alcohol systems with the average absolute deviations lower than 0.6%.The LLE data of two ternary systems, H2O-n-butanol-[bmim]PF6 and H2O-n-butanol-[omim]PF6, were further successfully predicted for the first time by using the NRTL binary parameters.
Ionic liquids have received increasing attention for their potential uses as non-volatile separation and reaction solvents, and the liquid-liquid equilibrium (LLE) of ionic liquid containing systems is of great importance for such practical applications. The NRTL (non-random two liquid) equation was extended and used in this paper for the calculation of the LLE data of some ionic liquid-alcohol binary systems. It was found that the extended NRTL model could be accurately used to represent the LLE of these ionic liquid-alcohol systems with the average absolute deviations lower than 0. 6 %. The LLE data of two ternary systems, H2O-n-butanol-[-bmim] PF6 and H2O n-butanol-[omim] PF6, were further successfully predicted for the first time by using the NRTL binary parameters.
出处
《化工学报》
EI
CAS
CSCD
北大核心
2006年第12期2801-2805,共5页
CIESC Journal
基金
江苏省基金面上项目(BK2005077)
南京大学人才引进启动项目(0205005137)
关键词
液液相平衡
离子液体
醇类
NRTL方程
liquid-liquid equilibrium
ionic liquid
alcohols
NRTL equation