Measurement and correlation of phase equilibrium data of the mixtures consisting of water, resorcinol, mesityl oxide at different temperatures

[1]  Chongxiong Duan,et al.  Facile Synthesis of Hierarchical Porous Metal-Organic Frameworks with Enhanced Catalytic Activity , 2018 .

[2]  Yun Chen,et al.  Screening solvents to extract phenol from aqueous solutions by the COSMO-SAC model and extraction process simulation , 2017 .

[3]  K. Xiong,et al.  Liquid–Liquid Equilibrium of Ternary Systems of Methyl Isobutyl Ketone + o-Cresol + Water at 298.2, 313.2 and 323.2 K , 2017, Journal of Solution Chemistry.

[4]  Yun Chen,et al.  Liquid phase equilibrium of the ternary systems, water + propionic or butyric acid + mesityl oxide, at (298.2 and 323.2) K , 2017 .

[5]  Yun Chen,et al.  Measurement, correlation and COSMO-SAC prediction of liquid-liquid equilibrium for the ternary systems, mesityl oxide + o-, m-, p-cresol + water, at 333.2K and 353.2 K , 2017 .

[6]  Yun Chen,et al.  Liquid-liquid equilibrium for ternary systems, methyl isobutyl ketone + (catechol, resorcinol and hydroquinone) + water at 333.15 K, 343.15 K and 353.15 K , 2017 .

[7]  Yun Chen,et al.  Determination and modeling of liquid-liquid equilibrium for ternary mixtures of methyl isopropyl ketone, cresol isomers and water , 2016 .

[8]  Yun Chen,et al.  Ternary liquid – Liquid equilibria for methyl isopropyl ketone + (resorcinol or hydroquinone) + water systems at different temperatures , 2016 .

[9]  Yun Chen,et al.  Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15 K, 343.15 K and 353.15 K: Experimental results and data correlation , 2016 .

[10]  Yun Chen,et al.  Liquid–Liquid Equilibria for the Ternary System Mesityl Oxide + Phenol + Water at 298.15, 313.15, and 323.15 K , 2016 .

[11]  Yun Chen,et al.  Measurement and Correlation of Liquid−Liquid Equilibria for the Ternary Methyl Isobutyl Ketone + Phenol + Water System at (333.15, 343.15 and 353.15) K under Atmospheric Pressure , 2016, Journal of Solution Chemistry.

[12]  N. Biswas,et al.  A Short Review of Techniques for Phenol Removal from Wastewater , 2016, Current Pollution Reports.

[13]  Yun Chen,et al.  Liquid–liquid equilibria in the ternary systems water+cresols+methyl butyl ketone at 298.2 and 313.2K: Experimental data and correlation , 2015 .

[14]  Ali Kargari,et al.  Phenol removal from industrial wastewaters: a short review , 2015 .

[15]  H. G. Gilani,et al.  Tie-line data for the aqueous solutions of phenol with organic solvents at T =298.2K , 2013 .

[16]  M. Aznar,et al.  (Liquid + liquid) equilibrium of {water + phenol + (1-butanol, or 2-butanol, or tert-butanol)} systems , 2010 .

[17]  M. R. Mafra,et al.  Liquid−Liquid Equilibrium of (Water + Acetone) with Cumene or α-Methylstyrene or Phenol at Temperatures of (323.15 and 333.15) K , 2006 .

[18]  M. R. Wolf-Maciel,et al.  Strategies for recovering phenol from wastewater: thermodynamic evaluation and environmental concerns , 2005 .

[19]  Hong Jiang,et al.  Studies on the extraction of phenol in wastewater. , 2003, Journal of hazardous materials.

[20]  I. Alnashef,et al.  Liquid-liquid equilibria of the ternary system water + acetic acid + 1-hexanol , 1997 .

[21]  E. Macedo,et al.  Liquid-liquid equilibria for ternary systems of water-phenol and solvents: data and representation with models , 1986 .

[22]  Aage Fredenslund,et al.  UNIFAC parameter table for prediction of liquid-liquid equilibriums , 1981 .

[23]  P. Singer,et al.  Assessment of coal conversion wastewaters: characterization and preliminary biotreatability. Report for November 1976-May 1978 , 1978 .

[24]  Yun Chen,et al.  Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone , 2017 .

[25]  Ye Xiao-jun Research on Liquid-Liquid Equilibrium of Water-Isopropyl Ether-Phenol and Water-Isobutanol-Phenol Systems , 2009 .

[26]  H. Dressler Resorcinol: Its Uses and Derivatives , 1994 .

[27]  D. C. Greminger,et al.  Solvent extraction of phenols from water , 1980 .

[28]  J. Prausnitz,et al.  Statistical thermodynamics of liquid mixtures: A new expression for the excess Gibbs energy of partly or completely miscible systems , 1975 .

[29]  J. Prausnitz,et al.  LOCAL COMPOSITIONS IN THERMODYNAMIC EXCESS FUNCTIONS FOR LIQUID MIXTURES , 1968 .

[30]  Irwin Bachman Tie Lines in Ternary Liquid Systems , 1940 .