Consistent vapour–liquid (VLE) and vapour–liquid–liquid (VLLE) data for the ternary system water (1) + ethanol (2) + n-heptane (3) are reported at 101.3 kPa at temperatures in the range of 341–352 K. An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in the determination of the VLLE. The experimental data indicates that a ternary heterogeneous azeotrope is present at 341.83K with a composition of 0.205, 0.432, and 0.363 mole fractions of water, ethanol, and heptane, respectively. The experimental results have been used to test the accuracy of the UNIFAC, UNIQUAC, and NRTL models in the calculation and prediction of the equilibrium data. None of these methods properly correlate and approximat...
Liquid-liquid equilibrium (LLE) data for the ternary systems of (water + formic acid + ethyl heptano...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in t...
An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in t...
Poster enviado a Equifase 2002, VI Iberoamerican Conference on Phase Equilibria for Process Design, ...
Isobaric vapor–liquid and vapor–liquid–liquid equilibria were measured for the water–ethanol–hexane ...
Isobaric vapour–liquid and vapour–liquid–liquid equilibrium data for the water + 1-butanol + toluene...
Poster enviado a Equifase 2006, VII Iberoamerican Conference on Phase Equilibria and Fluid Propertie...
The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liqu...
A method of parameters fitting to the experimental vapour - liquid - liquid equilibrium (VLLE) datai...
Liquid-liquid equilibrium (LLE) for the ternary (3-heptanone + phenol + water) system has been deter...
The (vapor + liquid), (liquid + liquid) and (vapor + liquid + liquid) equilibria of the ternary syst...
The (vapor + liquid), (liquid + liquid) and (vapor + liquid + liquid) equilibria of the ternary syst...
This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium ...
Liquid-liquid equilibrium (LLE) data for the ternary systems of (water + formic acid + ethyl heptano...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...
An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in t...
An all-glass, dynamic recirculating still equipped with an ultrasonic homogenizer has been used in t...
Poster enviado a Equifase 2002, VI Iberoamerican Conference on Phase Equilibria for Process Design, ...
Isobaric vapor–liquid and vapor–liquid–liquid equilibria were measured for the water–ethanol–hexane ...
Isobaric vapour–liquid and vapour–liquid–liquid equilibrium data for the water + 1-butanol + toluene...
Poster enviado a Equifase 2006, VII Iberoamerican Conference on Phase Equilibria and Fluid Propertie...
The temperature and the composition of the vapor–liquid–liquid equilibrium (VLLE) and the vapor–liqu...
A method of parameters fitting to the experimental vapour - liquid - liquid equilibrium (VLLE) datai...
Liquid-liquid equilibrium (LLE) for the ternary (3-heptanone + phenol + water) system has been deter...
The (vapor + liquid), (liquid + liquid) and (vapor + liquid + liquid) equilibria of the ternary syst...
The (vapor + liquid), (liquid + liquid) and (vapor + liquid + liquid) equilibria of the ternary syst...
This thesis comprises of two parts. The first part is the determination of vapor-liquid equilibrium ...
Liquid-liquid equilibrium (LLE) data for the ternary systems of (water + formic acid + ethyl heptano...
Liquid–liquid (L–L), solid–liquid (S–L), and solid–liquid–liquid (S–L–L) equilibrium data for the wa...
The liquid–liquid equilibrium of the water + 1-butanol + isoamyl alcohol system at 303.15 and 313.15...