Liquid–liquid equilibrium for the ternary system of isopropyl acetate + 2-propanol + glycerol at different temperatures under atmospheric pressure

2016 ◽  
Vol 412 ◽  
pp. 199-204 ◽  
Author(s):  
Yuan-Xiao Li ◽  
Qin Xu ◽  
Shi-Liang Liu ◽  
Hai-Ming Li ◽  
Feng-Bao Zhang ◽  
...  
Keyword(s):  
Ternary System ◽  
Atmospheric Pressure ◽  
Liquid Equilibrium ◽  
Isopropyl Acetate ◽  
Different Temperatures

Liquid–liquid equilibrium data for the systems {LTTM+benzene+hexane} and {LTTM+ethyl acetate+hexane} at different temperatures and atmospheric pressure

2013 ◽  
Vol 360 ◽  
pp. 54-62 ◽  
Author(s):  
Agustin S.B. Gonzalez ◽  
María Francisco ◽  
Guillermo Jimeno ◽  
Sara Lago García de Dios ◽  
Maaike C. Kroon
Keyword(s):  
Ethyl Acetate ◽  
Atmospheric Pressure ◽  
Liquid Equilibrium ◽  
Equilibrium Data ◽  
Different Temperatures

scholarly journals Gas-Liquid Equilibrium Prediction of Ternary System (CO2-Ethanol-Water) at Moderate Pressures and Different Temperatures Using SRK-EOS

2012 ◽  
Vol 2 (1) ◽  
pp. 1-5 ◽  
Author(s):  
Ghazi F. Najmuldeen ◽  
Ghassan Jasim Hadi ◽  
Arkan Jasim Hadi ◽  
Iqbal Ahmed
Keyword(s):  
Ternary System ◽  
Liquid Equilibrium ◽  
Different Temperatures

(Liquid + Liquid) Equilibrium for Ternary System of (Water + Phenol + Cyclohexane) at T = 298.2 K

2013 ◽  
Vol 3 (2) ◽  
pp. 75-84
Author(s):  
Hossein Ghanadzadeh ◽  
Milad Sangashekan ◽  
Shahin Asan
Keyword(s):  
Ternary System ◽  
Root Mean Square ◽  
Atmospheric Pressure ◽  
Distribution Coefficients ◽  
Mean Square ◽  
Liquid Equilibrium ◽  
Separation Factors ◽  
Experimental Solubility ◽  
Tie Line

Experimental solubility curves and tie-line data for the (water + phenol + 2-ethyl-1-hexanol) system was obtained at T = 298.2 K and atmospheric pressure. The tie-line data was determined by techniques karl-fischer and refractometry. This ternary system exhibits type-2 behavior of LLE. Distribution coefficients and separation factors were measured to evaluate the extracting ability of the solvent. The consistency of the experimental tie-line data was determined through the Othmer–Tobias and Bachman equations. The data were correlated with the NRTL (a = 0.25) and UNIQUAC models and the parameters estimated present root mean square deviations below 0.50%.

Liquid–Liquid Equilibrium for the Glycerol + Alcohol + Coconut Biodiesel System at Different Temperatures and Atmospheric Pressure

2012 ◽  
Vol 57 (12) ◽  
pp. 3557-3562 ◽  
Author(s):  
Francisca Maria R. Mesquita ◽  
Nathan Sombra Evangelista ◽  
Hosiberto Batista de Sant’Ana ◽  
Rílvia Saraiva de Santiago-Aguiar
Keyword(s):  
Atmospheric Pressure ◽  
Liquid Equilibrium ◽  
Different Temperatures
Sign in / Sign up

Export Citation Format

Share Document