Journal of South China University of Technology (Natural Science Edition) ›› 2006, Vol. 34 ›› Issue (8): 18-21,26.

• Chemistry & Chemical Engineering • Previous Articles     Next Articles

Liquid-Liquid Equilibrium for Sec-Butanol-Water-KF and Sec-Butanol-Water-K2CO3 Systems

Xu Wen-you1  Zhou Xiao-yun2  Wang Jing-yang2  Liu Wen-zheng2   

  1. 1.Key Laboratory of Chemical Manufacture Engineering,Yantai Univ.,Yantai 264005,Shandong,China;2.CNPC Lanzhou Petroleum and Chemical Corporation Solvent Factory,Lanzhou 730060,Gansu,China
  • Received:2005-11-08 Online:2006-08-25 Published:2006-08-25
  • Contact: 许文友(1963-),男,博士,教授,主要从事分离工程研究 E-mail:xuwenyou@ytu.edu.cn
  • About author:许文友(1963-),男,博士,教授,主要从事分离工程研究
  • Supported by:

    山东省科技攻关计划项目(2005GGA06705)

Abstract:

Both the water-rich phase(water phase)and the see-butanol-rich phase(see-butanol phase)can be form ed when adding KF or K2CO3 into the see-butanol-water system.In this paper,the data about the liquid-liquid equilibrium (LLE)of see-butanol-water-KF and see-butanol-water-K2CO3systems are measured at 25℃,showing that the see·-butanol phase contains negligible salt and the water phase contains negligible see-butanol when the
mass fraction of KF or K2CO3 in the water phase is not less than 26.38% or 28.76% ,respectively.Thus,water can be eficiently separated from the see-butanol-water system by adding KF or K2CO3 into the mixture.Moreover,a theoretical calculation of LLE data is carried out by using the Pitzer equation and the UNIQUAC equation to get the water activities respectively in the water phase and in the see-butanol phase.The calculated results are proved to be in good agreement with the experimental ones,the absolute mean deviations between the experimental data and the calculated results being 1.57% in the water phase and 0.33% in the see-butanol phase for see-butanol-wa-ter-KF system.and being 1.40% in the water phase and 0.39% in the sec-butanol phase for sec-butanol-water-K2CO3 system.

Key words: see-butanol-water-KF system, see-butanol-water-K2CO3 system, liquid-liquid equilibrium, Pitzer equation, UNIQUAC equation, theoretical calculation, separation