[1] Santesson S, Ramirez I B R, Viberg P, et al. Affinity two-phase partitioning in acoustically levitated drops [J]. Analytical Chemistry, 2004, 76(2): 303?308.
[2] Xu K, Wang Y, Huang Y, et al. A green deep eutectic solvent-based aqueous two-phase system for protein extracting [J]. Analytica Chimica Acta, 2015, 864(3): 9–20.
[3] Everberg H, Clough J, Henderson P, et al. Isolation of escherichia coli inner membranes by metal affinity two-phase partitioning [J]. Journal of Chromatography A, 2006, 1118(2): 244?252.
[4] Chen Y, Deng Y, Meng Y, et al. Partitioning equilibria and thermodynamics of gallium, indium, and thallium in aqueous two-phase systems [J]. Journal of Chemical and Engineering Data, 2015, 60(5): 1464?1468.
[5] Zhang Y, Sun T, HouU Q, et al. A green method for extracting molybdenum (VI) from aqueous solution with aqueous two-phase system without any extractant [J]. Separation and Purification Technology, 2016, 169(1): 151-157.
[6] Burcu T, Berna K, Leman T. Partitioning and purification of menadione induced NAD(P)H oxidase from Phanerochaete chrysosporium in aqueous two-phase systems [J]. Separation and Purification Technology, 2016, 163(2): 275–281.
[7] Carlos E A P, Paulo V F D, Franclsco C S J, et al. Recovery and concentration of ortho-phenylphenol from biodesulfurization of 4-methyl dibenzothiophene by aqueous two-phase flotation [J]. Separation and Purification Technology, 2017, 176(4): 306–312.
[8] Cui P, Wang T, Chen Y, et al. Density, viscosity, and surface tension of aqueous solution of 1, 4-bis- (2-hydroxypropyl) -piperazine sulfate [J]. Journal of Chemical and Engineering Data, 2013, 58(12): 3327–3331.
[9] Barbosa A A, Bonomo R C F, Martins C V, et al. Equilibrium data and physical properties of aqueous two phase systems formed by PEG (1500 and 4000) g·mol?1+ sodium sulfate + water at different temperatures and pH 2 [J]. Journal of Chemical and Engineering Data, 2016, 61, 3?11.
[10] Bonifacio P L, Aguiar C D, Alvarenga B G, et al. Phase diagrams for liquid?liquid equilibrium of aqueous two-phase system containing poly(ethylene glycol) (4000, 6000, or 10 000 g mol?1 + sodium hydrogen sulfite + Water) at different temperatures [J]. Journal of Chemical and Engineering Data, 2016, 61(6): 2062?2070.
[11] Alvarenga B G, Virtuoso L S, Lemes N H T, et al. Measurement and correlation of the phase equilibrium of aqueous two-phase systems composed of polyethylene(glycol) 1500 or 4000 + sodium sulfite + water at different temperatures[J]. Journal of Chemical and Engineering Data, 2014, 59 (2) :382–390.
[12] Virtuoso L S, Vello K A S F, Oliveira A A D, et al. Measurement and modeling of phase equilibrium in aqueous two phase systems: L35 + sodium citrate + water, L35 sodium tartrate + water, and L35 + sodium hydrogen sulfite + water at different temperatures[J]. Journal of Chemical and Engineering Data, 2012, 57 (2) :462–468.
[13] 国家环境保护总局. 固定污染源排气中二氧化硫的测定-碘量法: HJ/T 56-2000 [S]. 北京: 中国标准出版社, 2000.
State Environmental Protection Administration. Determination of Sulphur dioxide from exhausted gas of stationary source—Lodine titration method: HJ/T 56-2000 [S]. Beijing: Standards Press of China, 2000.
[14] 程浩. 无机离子对HPP-SO2吸收体系的影响与分离研究[D]. 合肥：合肥工业大学, 2016.
Cheng H. The relationship between the weight of a plant part and total weight as affected by plant density[D]. Hefei: Hefei University of Technology, 2016.
[15] Merechuk J C, Andrews B A, Asenjo J A. Aqueous two-phase systems for protein separation studies on phase inversion [J]. J Chromatogr B, 1998, 711(1-2): 285-293.
[16] Santos P L, Santos L N S, Ventura S P M, et al. Recovery of capsaicin from Capsicum frutescens by applying aqueous two-phase systems based on acetonitrile and cholinium-based ionic liquids[J]. Chemical Engineering Research and Design, 2016, 112(8): 103-112.
[17] Morandeiral L, Deive F J, Sanroman M A, et al. Aqueous two-phase systems containing imidazolium ionic liquids and a Tween surfactant[J]. J. Chem. Thermodynamics, 2017, 105: 209-216.
[18] Milosevic M, Staal K J J, Schuur B, et al. Experimental data and thermodynamic modeling of ternary aqueous biphasic systems of EO/PO polymers–Na2SO4–H2O [J]. Fluid Phase Equilibria, 2014, 366(2): 45-56.
[19] Guan Y, Lillry T H, Treery T E. A New excluded volume theory and its application to the coexistence curves of aqueous polymer two-phase systems [J]. Macromolecules 1993, 26(15): 3971-3979.
[20] Regupathi I, Monteiro S L. 1-Hexyl-3-Methylimidazolium chloride-potassium carbonate aqueous two phase system: equilibrium characteristics and BSA partitioning behavior[J]. Journal of Dispersion Science and Technology, 2014, 35 (3) :31-35.
[21] Taha M, Teng H L, Lee M J. Separation of tetrahydrofuran, 1,3-dioxolane, or 1,4-dioxane from their aqueous solutions using EPPS buffer at 298.15 K[J]. Separation and Purification Technology, 2013, 105 (5) :33-40.
[22] Lu Y, Cong B, Han J, et al. Measurement and correlation of phase equilibria in aqueous two-phase systems containing polyoxyethylenecetyl ether and potassium salt at different temperatures[J]. Journal of Chemical and Engineering Data, 2015, 60, 1193?1201.
[23] Othmer D F, Tobias P E. Tie-line correlation[J]. Industrial and Engineering Chemistry, 1942, 34(6): 693?696.
[24] Iyyaswami R, Shanon L M. 1-Hexyl-3-Methylimidazolium chloride-potassium carbonate aqueous two phase system: equilibrium characteristics and BSA partitioning behavior[J]. Journal of Dispersion Science and Technology, 35(3):418–427, 2014.
[25] 许文. 高等化工热力学[M]. 天津: 天津大学出版社, 2004: 183-184.
Xu W. Advanced Chemical Engineering Thermodynamics [M]. Tianjin: Tianjin University Press, 2004: 183-184.
[26] Renon H, Prausnitz J.M. Local compositions in thermodynamic excess function for liquid mixtures [J]. Aiche Journal, 1968, 14(1): 135-144.
