ABSTRACT

Total pressure measurements are reported for the ternary system 'di-isopropyl ether + 1-propanol + benzene' and two of the binary systems involved 'di-isopropyl ether + 1-propanol' and '1-propanol + benzene' at 313.15 K. Data reduction by Barker's method provides correlations for GE using the Margules equation for the binary systems and the Wohl expansion for the ternary system. Wilson, NRTL and UNIQUAC models have been applied successfully to both the binary and the ternary systems.

Compounds

#	Formula	Name
1	C6H14O	diisopropyl ether
2	C3H8O	propan-1-ol
3	C6H6	benzene

Datasets

The table above is generated from the ThermoML associated json file (link above). POMD and RXND refer to PureOrMixture and Reaction Datasets. The compound numbers are included in properties, variables, and phases, if specificied; the numbers refer to the table of compounds on the left.
Type	Compound-#	Property	Variable	Constraint	Phase	Method	#Points
POMD	1	Vapor or sublimation pressure, kPa ; Liquid		Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	4
POMD	2	Vapor or sublimation pressure, kPa ; Liquid		Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	2
POMD	3	Vapor or sublimation pressure, kPa ; Liquid		Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	2
POMD	2 1	Vapor or sublimation pressure, kPa ; Liquid	Mole fraction - 1; Liquid	Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	24
POMD	2 3	Vapor or sublimation pressure, kPa ; Liquid	Mole fraction - 3; Liquid	Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	26
POMD	2 3	Vapor or sublimation pressure, kPa ; Liquid	Mole fraction - 2; Liquid	Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	2
POMD	3 1	Vapor or sublimation pressure, kPa ; Liquid	Mole fraction - 1; Liquid	Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	2
POMD	2 3 1	Vapor or sublimation pressure, kPa ; Liquid	Mole fraction - 1; Liquid Mole fraction - 2; Liquid	Temperature, K; Liquid	Liquid Gas	Closed cell (Static) method	78

Thermodynamics Research Center / ThermoML | Fluid Phase Equilibria

Total pressure and excess Gibbs energy for the ternary mixture di-isopropyl ether + 1-propanol + benzene and its corresponding binary systems at 313.15K

Villamanan, R. M., Chamorro, C. R., Villamanan, M. A., Segovia, J. J.

ABSTRACT