In this work, liquid–liquid equilibria (LLE) data for the ternary system {mesityl oxide (1) + phenol (2) + water (3)} were measured at 298.15, 313.15, and 323.15 K under atmospheric pressure. The experimental LLE data were proven to be highly reliable by the Othmer–Tobias and Hand equations. The distribution coefficient and selectivity were calculated from the LLE data, which indicated mesityl oxide extracted phenol with a rather high efficiency. The NRTL and UNIQUAC models were employed to correlate the LLE data, yielding binary interaction parameters for simulating relevant extraction processes. The experimental LLE data were correlated successfully by both models
Liquid–liquid equilibria of the ternary system water + tetradecane + 2-butyloxyethanol in the temper...
© 2015 Dr. Zheng LiSolvent extraction is a separation technique widely used in a variety of industri...
International audienceLiquid–liquid equilibrium data for the ternary system water + 1-propanol + 1-p...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
1-Dodecanol with low solubility in water is a potential solvent to extract phenol from wastewater. T...
Liquid-liquid equilibrium (LLE) for the ternary (3-heptanone + phenol + water) system has been deter...
Experimental liquid–liquid equilibria (LLE) data for ternary (methyl propyl ketone + hydroquinone + ...
Liquid–liquid equilibrium (LLE) data for the ternary system water + benzyl alcohol + methylbenzene w...
In this work, liquid–liquid phase equilibria (LLE) data for the ternary system, water + acetic acid ...
Funding Information: Roshi Dahal acknowledges Fortum and Neste Foundation for the financial support....
In this work, experimental liquid-liquid equilibrium data for the ternary system water + acrylic aci...
Liquid–liquid equilibrium (LLE) data for the ternary systems (methyl isobutyl ketone + quinoline or ...
Liquid-liquid equilibria for the ternary systems water + acetic acid + ethyl acetate and water + ace...
Liquid–liquid equilibria of the ternary system water + tetradecane + 2-butyloxyethanol in the temper...
© 2015 Dr. Zheng LiSolvent extraction is a separation technique widely used in a variety of industri...
International audienceLiquid–liquid equilibrium data for the ternary system water + 1-propanol + 1-p...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
To provide essential data for the separation of diethoxymethane and system water using mesityl oxide...
1-Dodecanol with low solubility in water is a potential solvent to extract phenol from wastewater. T...
Liquid-liquid equilibrium (LLE) for the ternary (3-heptanone + phenol + water) system has been deter...
Experimental liquid–liquid equilibria (LLE) data for ternary (methyl propyl ketone + hydroquinone + ...
Liquid–liquid equilibrium (LLE) data for the ternary system water + benzyl alcohol + methylbenzene w...
In this work, liquid–liquid phase equilibria (LLE) data for the ternary system, water + acetic acid ...
Funding Information: Roshi Dahal acknowledges Fortum and Neste Foundation for the financial support....
In this work, experimental liquid-liquid equilibrium data for the ternary system water + acrylic aci...
Liquid–liquid equilibrium (LLE) data for the ternary systems (methyl isobutyl ketone + quinoline or ...
Liquid-liquid equilibria for the ternary systems water + acetic acid + ethyl acetate and water + ace...
Liquid–liquid equilibria of the ternary system water + tetradecane + 2-butyloxyethanol in the temper...
© 2015 Dr. Zheng LiSolvent extraction is a separation technique widely used in a variety of industri...
International audienceLiquid–liquid equilibrium data for the ternary system water + 1-propanol + 1-p...