Dielectric behavior of the ternary systems of toluene, chlorobenzene, and 1-hexanol with n-hexane-benzyl alcohol as their partially miscible binary subsystem

1986 ◽  
Vol 31 (1) ◽  
pp. 112-115 ◽  
Author(s):  
Ramesh P. Singh ◽  
Chandreshwar P. Sinha ◽  
Basuki N. Singh
Keyword(s):  
Benzyl Alcohol ◽  
Ternary Systems ◽  
Dielectric Behavior ◽  
Binary Subsystem ◽  
Partially Miscible

Measurement of the Viscosity of Binary and Ternary Systems Containing Benzaldehyde, Toluene, and Benzyl Alcohol at 293.15 K and 0.1 MPa

2002 ◽  
Vol 47 (4) ◽  
pp. 927-931 ◽  
Author(s):  
Raphael da C. Cruz ◽  
Rosana J. Martins ◽  
Márcio J. E. de M. Cardoso ◽  
Oswaldo E. Barcia
Keyword(s):  
Benzyl Alcohol ◽  
Ternary Systems ◽  
Binary And Ternary Systems

Composition Routes for Three-Phase Partially Miscible Flow in Ternary Systems

SPE Journal ◽  
2005 ◽  
Vol 10 (02) ◽  
pp. 161-174 ◽  
Author(s):  
Tara C. LaForce ◽  
Russell T. Johns
Keyword(s):  
Ternary Systems ◽  
Miscible Flow ◽  
Three Phase ◽  
Partially Miscible

Correlation of the liquid–liquid equilibrium data for specific ternary systems with one or two partially miscible binary subsystems

2009 ◽  
Vol 278 (1-2) ◽  
pp. 9-14 ◽  
Author(s):  
J.A. Reyes-Labarta ◽  
M.M. Olaya ◽  
R. Velasco ◽  
M.D. Serrano ◽  
A. Marcilla
Keyword(s):  
Ternary Systems ◽  
Liquid Equilibrium ◽  
Partially Miscible ◽  
Equilibrium Data

Some information on calculating the liquid-liquid equilibrium of ternary systems. an improvement of prediction of liquid-liquid equilibrium in ternary systems from binary equilibrium data

1982 ◽  
Vol 47 (5) ◽  
pp. 1420-1432 ◽  
Author(s):  
Július Surový ◽  
Ján Dojčanský ◽  
Soňa Bafrncová
Keyword(s):  
Polar Solvent ◽  
Ternary Systems ◽  
Correct Prediction ◽  
Liquid Equilibrium ◽  
Partially Miscible ◽  
Nrtl Equation ◽  
Equilibrium Data ◽  
Solvent Systems ◽  
Kister Equation ◽  
Mutual Solubilities

A possibility is described of improving the prediction of ternary liquid-liquid equilibrium data from binary ones by using three-parameter equations for calculating activity coefficients. The parameters for completely miscible pairs of liquids were determined from their vapour-liquid equilibrium data and those for partially miscible pairs of liquids from their mutual solubilities and from one limiting activity coefficient. A quantitatively correct prediction of the liquid-liquid equilibrium data was achieved in all cases by means of three different equations (NRTL equation, Redlich-Kister equation and Wilson equation modified by Novák and coworkers) in four hydrocarbon-hydrocarbon-polar solvent systems investigated.

HEAT TRANSFER IN PARTIALLY MISCIBLE TERNARY SYSTEMS

1988 ◽  
Vol 64 (1) ◽  
pp. 1-11
Author(s):  
TSAN-YUE YANG ◽  
GEORGE E. KLINZING ◽  
SHIAO-HUNG CHIANG ◽  
FERNANDO J. AGUIRRE
Keyword(s):  
Heat Transfer ◽  
Ternary Systems ◽  
Partially Miscible
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