Liquid−Liquid Equilibrium Data for Systems Containing Vegetable Oils, Anhydrous Ethanol, and Hexane at (313.15, 318.15, and 328.15) K

2009 ◽  
Vol 54 (6) ◽  
pp. 1850-1859 ◽  
Author(s):  
Marcelo Lanza ◽  
Guilherme Sanaiotti ◽  
Eduardo A. C. Batista ◽  
Ronei J. Poppi ◽  
Antonio J. A. Meirelles
Keyword(s):  
Vegetable Oils ◽  
Anhydrous Ethanol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Liquid−Liquid Equilibrium Data for Fatty Systems Containing Refined Rice Bran Oil, Oleic Acid, Anhydrous Ethanol, and Hexane

2009 ◽  
Vol 54 (8) ◽  
pp. 2174-2181 ◽  
Author(s):  
Wagner L. Priamo ◽  
Marcelo Lanza ◽  
Antonio J. A. Meirelles ◽  
Eduardo A. C. Batista
Keyword(s):  
Oleic Acid ◽  
Rice Bran ◽  
Rice Bran Oil ◽  
Anhydrous Ethanol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Liquid–Liquid Equilibrium Data for Systems Involving Triacylglycerols from (Soybean, Cottonseed, or Rice Bran) Oil + Partial Acylglycerols + Anhydrous Ethanol at T = 303.2 and 318.2 K

2019 ◽  
Vol 64 (5) ◽  
pp. 2153-2162 ◽  
Author(s):  
Simone Shiozawa ◽  
Marcela C. Ferreira ◽  
Daniel Gonçalves ◽  
Antonio J. A. Meirelles ◽  
Eduardo A. C. Batista
Keyword(s):  
Rice Bran ◽  
Rice Bran Oil ◽  
Anhydrous Ethanol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Liquid−Liquid Equilibrium Data for Systems Containing Refined Rice Bran Oil, Anhydrous Ethanol, Water, and Hexane

2009 ◽  
Vol 54 (8) ◽  
pp. 2182-2188 ◽  
Author(s):  
Irede Dalmolin ◽  
Marcelo Lanza ◽  
Antonio J. A. Meirelles ◽  
Eduardo A. C. Batista
Keyword(s):  
Rice Bran ◽  
Rice Bran Oil ◽  
Anhydrous Ethanol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Liquid−Liquid Equilibrium Data for Systems ContainingJatropha curcasOil + Oleic Acid + Anhydrous Ethanol + Water at (288.15 to 318.15) K

2010 ◽  
Vol 55 (7) ◽  
pp. 2416-2423 ◽  
Author(s):  
César A. S. da Silva ◽  
Guilherme Sanaiotti ◽  
Marcelo Lanza ◽  
Antonio J. A. Meirelles ◽  
Eduardo A. C. Batista
Keyword(s):  
Oleic Acid ◽  
Anhydrous Ethanol ◽  
Liquid Equilibrium ◽  
Equilibrium Data

Isothermal and isobaric vapour-liquid equilibrium data in the tetrachloromethane-sec-butyl alcohol system

1983 ◽  
Vol 48 (9) ◽  
pp. 2446-2453 ◽  
Author(s):  
Jan Linek
Keyword(s):  
Experimental Data ◽  
Boiling Point ◽  
Butyl Alcohol ◽  
Correlation Equations ◽  
Wilson Equation ◽  
Liquid Equilibrium ◽  
Raoult’S Law ◽  
System A ◽  
Equilibrium Data ◽  
Alcohol System

Isothermal vapour-liquid equilibrium data at 65, 73 and 80 °C and isobaric ones at 101.3 kPa were measured in the tetrachloromethane-sec-butyl alcohol system. A modified circulation still of the Gillespie type was used for the measurements. Under the conditions of measurement, the system exhibits positive deviations from Raoult's law and minimum boiling-point azeotropes. The experimental data were fitted to a number of correlation equations, the most suitable being the Wilson equation.

Vapour-liquid equilibrium in the ternary system cyclohexane-acetic acid-propionic acid

1989 ◽  
Vol 54 (11) ◽  
pp. 2840-2847 ◽  
Author(s):  
Ivona Malijevská ◽  
Alena Maštalková ◽  
Marie Sýsová
Keyword(s):  
Acetic Acid ◽  
Ternary System ◽  
Propionic Acid ◽  
Activity Coefficients ◽  
Error Propagation ◽  
Analytical Techniques ◽  
Liquid Equilibrium ◽  
Consistency Test ◽  
Propagation Law ◽  
Equilibrium Data

Isobaric equilibrium data (P = 101.3 kPa) for the system cyclohexane-acetic acid-propionic acid have been measured by two different analytical techniques. Activity coefficients calculated by simultaneous solving of equations for the chemical and phase equilibria were subjected to a consistency test based on inaccuracies determined from the error propagation law, and were correlated by Wilson’s equation. The activity coefficients measured were compared with those calculated from binary vapour-liquid equilibrium data and with values predicted by the UNIFAC method.

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