ABSTRACT

Viscosities for the binary mixtures of isomeric butanols or isomeric chlorobutanes with 2-methyltetrahydrofuran were determined at the temperatures of 298.15 K and 313.15 K; the viscosities of the mixture 2-methyl-2-chloropropane with 2-methyltetrahydrofuran were measured only at 298.15 K. The viscosity data were correlated by the the McAllister equation. Viscosity deviations for the mixtures containing isomeric butanols are negative over the whole composition range. On the other hand for the mixtures involving isomeric chlorobutanes, viscosity deviations are slightly negative except for 1-chlorobutane, in this case viscosity deviations present inversion of sign.

Compounds

#	Formula	Name
1	C4H10O	butan-1-ol
2	C4H10O	butan-2-ol
3	C4H10O	2-methyl-1-propanol
4	C4H10O	2-methylpropan-2-ol
5	C4H9Cl	1-chlorobutane
6	C4H9Cl	2-chlorobutane
7	C4H9Cl	1-chloro-2-methylpropane
8	C4H9Cl	2-chloro-2-methylpropane
9	C5H10O	2-methyltetrahydrofuran

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	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	1	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	2	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	2	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	3	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	3	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	4	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	4	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	5	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	5	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	6	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	6	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	7	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	7	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	8	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Pressure, kPa; Liquid		Liquid	CAPTUB::UFactor:2	1
POMD	8	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Pressure, kPa; Liquid		Liquid	VIBTUB::UFactor:2	1
POMD	9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB::UFactor:4	2
POMD	9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB::UFactor:2	2
POMD	1 9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 1; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	1 9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 1; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	2 9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 2; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	2 9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 2; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	3 9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 3; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	3 9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 3; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	4 9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 4; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	4 9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 4; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	9 5	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 5; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	9 5	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 5; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	6 9	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 6; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	6 9	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 6; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	9 7	Kinematic viscosity, m2/s ; Liquid	Temperature, K; Liquid Mole fraction - 7; Liquid	Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:4	26
POMD	9 7	Mass density, kg/m3 ; Liquid	Temperature, K; Liquid Mole fraction - 7; Liquid	Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	26
POMD	9 8	Kinematic viscosity, m2/s ; Liquid	Mole fraction - 8; Liquid	Temperature, K; Liquid Pressure, kPa; Liquid	Liquid	CAPTUB:UFactor:2	13
POMD	9 8	Mass density, kg/m3 ; Liquid	Mole fraction - 8; Liquid	Temperature, K; Liquid Pressure, kPa; Liquid	Liquid	VIBTUB:UFactor:2	13

Thermodynamics Research Center / ThermoML | Journal of Chemical and Engineering Data

Viscosities of Binary Mixtures of Isomeric Butanols or Isomeric Chlorobutanes with 2-Methyltetrahydrofuran

Giner, B.[Beatriz], Aldea, M. E., Martinez, S.[Santiago], Gascon, I.[Ignacio], Lafuente, C.[Carlos]

ABSTRACT