4ZHAO Jun-ming(赵俊明).Simulation and optimization of the reactive extraction process for MEKO production with HPO process(磷酸羟胺法制丁酮肟反应萃取过程的模拟与优化)[D].Shanghai(上海):East China University of Science and Technology(华东理工大学),2013.
5Huddleston J G,Willauer H D,Swatloski R P,et al.Room temperature ionic liquids as novel media for‘clean’liquid-liquid extraction[J].Chemical Communications,1998(16):1765-1766.
6Seddon K R.Ionic liquids for clean technology[J].Journal of Chemical Technology and Biotechnology,1997,68(4):351-356.
7Liu J F,Chi Y G,Jiang G B.Screening the extractability of some typical environmental pollutants by ionic liquids in liquid-phase micro-extraction[J].Journal of Separation Science,2005,28(1):87-91.
8Pereiro A B,Araújo J M M,Oliveira F S S,et al.Solubility of inorganic salts in pure ionic liquids[J].The Journal of Chemical Thermodynamics,2012,55(12):29-36.
9Bachman I.Tie lines in ternary liquid systems[J].Industrial and Engineering Chemistry,Analytical Edition,1940,12(1):38-39.
10Xu D M,Wu C X,Zhang Q,et al.Liquid–liquid equilibrium for the ternary systems water+2-methyl-1-propanol+butyl acetate and water+2-methyl-2-propanol+butyl acetate at(298.15 and 323.15)K[J].Fluid Phase Equilibria,2014,381(11):60-66.
