This paper reports the measurements of liquid + liquid, solid + liquid and solid + liquid + liquid equilibrium data of the water + 2-propanol + 1-undecanol ternary system at temperatures from 275.15 to 288.15 K. The three isothermal phase diagrams show different regions depending on temperature. At 288.15 K a liquid + liquid region is observed, however, below this temperature, solid phases appear. The experimental data have been compared with the ternary water + ethanol + 1-undecanol system at the same temperatures; some differences arise in the shapes of the different regions. Finally, by means of the distribution and selectivity coefficients, the capability of the 1-undecanol as an extractant agent in alcohol dewatering has been analyzed....
In this work, the liquid-liquid equilibrium data of the system water + 1-butanol + 2-butanol was stu...
The SLLV phase equilibria of the water + NaCl + 2-propanol mixture have been determined experimental...
(Liquid + liquid) equilibrium (LLE) data of the solubility (binodal) curves and tie-line end composi...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The process of recovery by liquid–liquid extraction of ethanol manufactured in a fermentation proces...
Isobaric vapour–liquid and vapour–liquid–liquid equilibrium data for the water + 1-butanol + toluene...
The experimental liquid-liquid equilibria of a water-ethanol-1-dodecanol system were investigated at...
Póster presentado en "10th Mediterranean Congress of Chemical Engineering", Barcelona, November 15-1...
The phase-forming ability of KCl in propanols has been investigated, aiming to assess its utility in...
Equilibrium data for the water + 1-butanol + 2-octanol system is determined in this work. Liquid-liq...
Aqueous two-phase systems involve a limited region of a complicated phase diagram usually containing...
Recovery of propionic acid from aqueous solution is economically and environmentally important. In t...
Isobaric vapor-liquid-liquid-solid equilibria for the ternary system water + sodium chloride + 1-pro...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
Experimental equilibrium data of the systems water + NaCl or KCl+ 2-methyl 2-propanol are determined...
In this work, the liquid-liquid equilibrium data of the system water + 1-butanol + 2-butanol was stu...
The SLLV phase equilibria of the water + NaCl + 2-propanol mixture have been determined experimental...
(Liquid + liquid) equilibrium (LLE) data of the solubility (binodal) curves and tie-line end composi...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The process of recovery by liquid–liquid extraction of ethanol manufactured in a fermentation proces...
Isobaric vapour–liquid and vapour–liquid–liquid equilibrium data for the water + 1-butanol + toluene...
The experimental liquid-liquid equilibria of a water-ethanol-1-dodecanol system were investigated at...
Póster presentado en "10th Mediterranean Congress of Chemical Engineering", Barcelona, November 15-1...
The phase-forming ability of KCl in propanols has been investigated, aiming to assess its utility in...
Equilibrium data for the water + 1-butanol + 2-octanol system is determined in this work. Liquid-liq...
Aqueous two-phase systems involve a limited region of a complicated phase diagram usually containing...
Recovery of propionic acid from aqueous solution is economically and environmentally important. In t...
Isobaric vapor-liquid-liquid-solid equilibria for the ternary system water + sodium chloride + 1-pro...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
Experimental equilibrium data of the systems water + NaCl or KCl+ 2-methyl 2-propanol are determined...
In this work, the liquid-liquid equilibrium data of the system water + 1-butanol + 2-butanol was stu...
The SLLV phase equilibria of the water + NaCl + 2-propanol mixture have been determined experimental...
(Liquid + liquid) equilibrium (LLE) data of the solubility (binodal) curves and tie-line end composi...