Property
Value
Unit
Temperature (K)
Source
Cp,gas [207.74; 259.87]
J/mol×K
[429.06; 590.24]
Cp,gas 207.74
J/mol×K
429.06
Joback Calculated Property
Cp,gas 217.26
J/mol×K
455.92
Joback Calculated Property
Cp,gas 226.43
J/mol×K
482.79
Joback Calculated Property
Cp,gas 235.27
J/mol×K
509.65
Joback Calculated Property
Cp,gas 243.79
J/mol×K
536.51
Joback Calculated Property
Cp,gas 251.98
J/mol×K
563.38
Joback Calculated Property
Cp,gas 259.87
J/mol×K
590.24
Joback Calculated Property
Cp,liquid [232.46; 249.15]
J/mol×K
[290.01; 303.74]
Cp,liquid 232.46
J/mol×K
290.01
NIST
Cp,liquid 236.50
J/mol×K
293.15
NIST
Cp,liquid 236.50
J/mol×K
293.15
NIST
Cp,liquid 244.80
J/mol×K
298.00
NIST
Cp,liquid 239.62
J/mol×K
298.15
NIST
Cp,liquid 239.68
J/mol×K
298.15
NIST
Cp,liquid 243.20
J/mol×K
298.15
NIST
Cp,liquid 241.32
J/mol×K
298.15
NIST
Cp,liquid 240.65
J/mol×K
298.15
NIST
Cp,liquid 240.57
J/mol×K
298.15
NIST
Cp,liquid 237.85
J/mol×K
298.15
NIST
Cp,liquid 241.32
J/mol×K
298.15
NIST
Cp,liquid 242.50
J/mol×K
298.15
NIST
Cp,liquid 249.15
J/mol×K
300.61
NIST
Cp,liquid 247.70
J/mol×K
303.74
NIST
η [0.0014110; 0.0074590]
Pa×s
[283.15; 343.15]
η 0.0074590
Pa×s
283.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0053350
Pa×s
293.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0054120
Pa×s
293.15
A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η 0.0045960
Pa×s
298.15
A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η 0.0045940
Pa×s
298.15
Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0046050
Pa×s
298.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0046426
Pa×s
298.15
Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0038290
Pa×s
303.15
Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η 0.0039985
Pa×s
303.15
Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0038290
Pa×s
303.15
Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η 0.0039170
Pa×s
303.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0038870
Pa×s
303.15
Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0039440
Pa×s
303.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0037630
Pa×s
303.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0039640
Pa×s
303.15
A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η 0.0033590
Pa×s
308.15
Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0033180
Pa×s
308.15
Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η 0.0034140
Pa×s
308.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0034713
Pa×s
308.15
Densities, Viscosities, and Volumetric Properties of Binary Mixtures of 1,2-Propanediol + 1-Heptanol or 1-Hexanol and 1,2-Ethanediol + 2-Butanol or 2-Propanol at T = (298.15, 303.15, and 308.15) K
η 0.0029600
Pa×s
313.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0028790
Pa×s
313.15
Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η 0.0029660
Pa×s
313.15
A Study on Properties Derived from Densities and Viscosities for the Ternary Systems (Methyl Pentanoate or Methyl Heptanoate) + n-Octane + 1-Hexanol and their Binary Subsystems at Various Temperatures.
η 0.0029140
Pa×s
313.15
Acoustical and Excess Properties of {Chlorobenzene + 1-Hexanol, or 1-Heptanol, or 1-Octanol, or 1-Nonanol, or 1-Decanol} at (298.15, 303.15, 308.15, and 313.15) K
η 0.0029370
Pa×s
313.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0028790
Pa×s
313.15
Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η 0.0025180
Pa×s
318.15
Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η 0.0025810
Pa×s
318.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0022760
Pa×s
323.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0022150
Pa×s
323.15
Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
η 0.0022510
Pa×s
323.15
Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
η 0.0022150
Pa×s
323.15
Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
η 0.0021720
Pa×s
323.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0016540
Pa×s
333.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
η 0.0014110
Pa×s
343.15
Densities and Viscosities for Binary and Ternary Mixtures of 1, 4-Dioxane + 1-Hexanol + N,N-Dimethylaniline from T ) (283.15 to 343.15) K
εr 13.06
298.15
Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
Δfus H [15.38; 15.48]
kJ/mol
[225.80; 225.80]
Δfus H 15.38
kJ/mol
225.80
NIST
Δfus H 15.48
kJ/mol
225.80
NIST
Δfus H 15.48
kJ/mol
225.80
NIST
Δvap H [44.50; 62.00]
kJ/mol
[295.50; 430.50]
Δvap H 61.20
kJ/mol
295.50
NIST
Δvap H 62.00
kJ/mol
296.50
NIST
Δvap H 61.90 ± 0.20
kJ/mol
300.50
NIST
Δvap H 57.70
kJ/mol
320.50
NIST
Δvap H 58.50 ± 0.20
kJ/mol
328.00
NIST
Δvap H 57.60 ± 0.20
kJ/mol
343.00
NIST
Δvap H 56.00
kJ/mol
357.50
NIST
Δvap H 55.20 ± 0.20
kJ/mol
358.00
NIST
Δvap H 59.70
kJ/mol
364.00
NIST
Δvap H 53.80 ± 0.20
kJ/mol
368.00
NIST
Δvap H 57.90
kJ/mol
369.00
NIST
Δvap H 58.50
kJ/mol
378.00
NIST
Δvap H 57.90
kJ/mol
379.00
NIST
Δvap H 51.40
kJ/mol
393.00
NIST
Δvap H 47.90
kJ/mol
398.50
NIST
Δvap H 48.53
kJ/mol
430.30
KDB
Δvap H 44.50
kJ/mol
430.50
NIST
ν [0.0000036; 0.0000047]
m2 /s
[303.15; 313.15]
ν 0.0000047
m2 /s
303.15
Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
ν 0.0000036
m2 /s
313.15
Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Pentan-1-ol, Hexan-1-ol, and Heptan-1-ol at (303.15 and 313.15) K
Pvap [1.43e-04; 106.98]
kPa
[237.95; 432.32]
Pvap 1.43e-04
kPa
237.95
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.43e-04
kPa
238.00
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.45e-04
kPa
238.00
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 2.96e-04
kPa
243.20
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 2.96e-04
kPa
243.20
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 2.93e-04
kPa
243.25
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 5.69e-04
kPa
248.20
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 5.60e-04
kPa
248.20
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 5.64e-04
kPa
248.20
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.06e-03
kPa
253.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.05e-03
kPa
253.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.05e-03
kPa
253.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.92e-03
kPa
258.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.92e-03
kPa
258.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 1.92e-03
kPa
258.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 3.39e-03
kPa
263.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 3.39e-03
kPa
263.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 3.38e-03
kPa
263.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 4.68e-03
kPa
265.00
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 5.84e-03
kPa
268.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 5.84e-03
kPa
268.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 5.84e-03
kPa
268.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 6.64e-03
kPa
268.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 9.87e-03
kPa
273.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 9.86e-03
kPa
273.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 9.87e-03
kPa
273.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.01
kPa
273.40
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.01
kPa
273.65
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.01
kPa
273.65
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.01
kPa
273.65
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.02
kPa
278.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.02
kPa
278.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.02
kPa
278.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.02
kPa
278.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.03
kPa
283.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.03
kPa
283.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.03
kPa
283.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.03
kPa
283.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.05
kPa
288.10
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.04
kPa
288.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.04
kPa
288.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.04
kPa
288.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.07
kPa
293.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.07
kPa
293.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.07
kPa
293.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.07
kPa
293.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.07
kPa
293.30
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.10
kPa
298.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.12
kPa
298.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.10
kPa
298.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.10
kPa
298.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.12
kPa
298.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.11
kPa
298.30
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.15
kPa
303.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.17
kPa
303.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.15
kPa
303.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.15
kPa
303.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.17
kPa
303.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.17
kPa
303.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.17
kPa
303.30
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.22
kPa
308.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.25
kPa
308.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.22
kPa
308.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.22
kPa
308.15
Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
Pvap 0.25
kPa
308.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.25
kPa
308.30
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.30
kPa
310.40
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.36
kPa
313.10
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.36
kPa
313.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.37
kPa
313.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.52
kPa
318.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.53
kPa
318.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.53
kPa
318.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.73
kPa
323.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 0.71
kPa
323.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 0.75
kPa
323.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 1.03
kPa
328.10
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 1.01
kPa
328.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.01
kPa
328.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 1.43
kPa
333.10
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 1.40
kPa
333.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.46
kPa
333.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 1.90
kPa
338.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 1.98
kPa
338.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 2.54
kPa
343.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 2.64
kPa
343.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 2.04
kPa
343.46
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.16
kPa
344.20
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.23
kPa
344.60
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.35
kPa
345.36
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.47
kPa
346.17
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.67
kPa
347.27
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 2.79
kPa
348.10
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.38
kPa
348.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 3.48
kPa
348.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 2.85
kPa
348.35
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.04
kPa
349.38
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.11
kPa
349.75
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.32
kPa
350.75
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.44
kPa
351.39
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.64
kPa
352.20
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.73
kPa
352.63
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.83
kPa
353.00
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 4.43
kPa
353.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 4.64
kPa
353.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 3.89
kPa
353.31
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 3.96
kPa
353.82
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 4.31
kPa
355.20
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 4.79
kPa
357.01
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 5.79
kPa
357.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 5.76
kPa
358.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 6.13
kPa
358.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 5.15
kPa
358.22
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 5.51
kPa
359.43
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 5.79
kPa
360.34
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 6.04
kPa
361.12
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 6.29
kPa
361.86
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 7.41
kPa
363.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 7.87
kPa
363.20
Measurement and Prediction of Thermochemical Properties. Improved Benson-Type Increments for the Estimation of Enthalpies of Vaporization and Standard Enthalpies of Formation of Aliphatic Alcohols
Pvap 6.99
kPa
363.85
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 7.27
kPa
364.61
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 7.64
kPa
365.58
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 7.92
kPa
366.30
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.32
kPa
366.67
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 8.40
kPa
367.44
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 8.67
kPa
368.05
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.44
kPa
368.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 9.08
kPa
368.99
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.40
kPa
369.67
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.67
kPa
370.24
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 9.95
kPa
370.83
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 10.27
kPa
371.45
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 10.59
kPa
372.10
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.06
kPa
372.64
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 11.05
kPa
373.00
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.91
kPa
373.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 11.43
kPa
373.67
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 11.73
kPa
374.19
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 12.27
kPa
375.14
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 12.73
kPa
375.93
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 13.15
kPa
376.59
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 13.53
kPa
377.22
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 13.87
kPa
377.56
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 13.71
kPa
377.83
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 13.85
kPa
378.01
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.90
kPa
378.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 14.15
kPa
378.37
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.40
kPa
378.72
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.65
kPa
379.10
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 14.91
kPa
379.46
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 15.12
kPa
379.75
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 15.37
kPa
380.06
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 15.61
kPa
380.41
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 15.95
kPa
380.87
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.15
kPa
381.15
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.37
kPa
381.45
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.77
kPa
381.80
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 16.77
kPa
381.81
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 16.71
kPa
381.89
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 16.97
kPa
382.25
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 17.21
kPa
382.56
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 17.44
kPa
382.85
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.50
kPa
383.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 17.69
kPa
383.18
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 17.84
kPa
383.34
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.09
kPa
383.67
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 18.43
kPa
384.08
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 19.05
kPa
384.87
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 19.47
kPa
385.37
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 19.91
kPa
385.86
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 20.26
kPa
386.17
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 20.31
kPa
386.31
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 20.79
kPa
386.83
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 21.15
kPa
387.23
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 21.48
kPa
387.62
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 21.91
kPa
388.10
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 22.79
kPa
388.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 22.37
kPa
388.59
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 22.79
kPa
389.05
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 23.20
kPa
389.48
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 23.60
kPa
389.89
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 23.95
kPa
390.23
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 24.36
kPa
390.65
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 24.54
kPa
390.77
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 24.54
kPa
390.78
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 24.67
kPa
390.93
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 25.00
kPa
391.07
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 25.13
kPa
391.40
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 25.51
kPa
391.75
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 25.83
kPa
392.06
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 26.31
kPa
392.51
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 26.59
kPa
392.77
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 27.00
kPa
393.14
Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
Pvap 27.86
kPa
393.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 29.35
kPa
395.23
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 29.35
kPa
395.23
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 30.00
kPa
395.62
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 33.84
kPa
398.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 34.77
kPa
399.57
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 35.00
kPa
399.65
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 40.00
kPa
402.36
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 40.00
kPa
403.15
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 40.85
kPa
403.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 40.02
kPa
403.66
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 40.70
kPa
403.73
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 45.00
kPa
406.36
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 48.72
kPa
407.89
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 47.57
kPa
407.98
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 49.02
kPa
408.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 50.00
kPa
409.25
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 55.00
kPa
411.92
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 58.50
kPa
413.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 58.84
kPa
413.31
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 60.00
kPa
414.44
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 60.20
kPa
414.61
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 65.00
kPa
416.75
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 69.49
kPa
418.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 69.27
kPa
418.35
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 70.00
kPa
418.98
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 74.69
kPa
420.99
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 75.00
kPa
421.05
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 77.40
kPa
421.90
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 80.00
kPa
423.01
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 82.16
kPa
423.15
Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
Pvap 85.00
kPa
424.87
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 85.63
kPa
425.15
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 90.00
kPa
426.69
Phase Equlibria for Hexyl Acetate Reactive Distillation
Pvap 92.07
kPa
427.54
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 93.19
kPa
427.85
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 93.26
kPa
427.90
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 99.78
kPa
429.19
Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
Pvap 98.12
kPa
429.52
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 98.16
kPa
429.54
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 101.30
kPa
430.11
Vapor-liquid equilibrium data of binary mixtures of 1-hexanol, 1-heptanol, 1-nonanol and 1,3-propanediol at P = 101.3 kPa using differential scanning calorimetry (DSC)
Pvap 105.46
kPa
431.85
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 106.75
kPa
432.25
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
Pvap 106.98
kPa
432.32
Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
n 0 [1.41270; 1.42070]
[293.10; 313.15]
n 0 1.41800
293.10
Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
n 0 1.41750
293.15
Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
n 0 1.41830
293.15
Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n 0 1.41826
293.15
Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
n 0 1.41807
293.15
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n 0 1.41780
293.15
Densities, Viscosities, Speeds of Sound, and Refractive Indices for Binary Mixtures of Diethylcarbonate, Acetophenone, and 1-Hexanol at (293.15, 303.15, 313.15, and 323.15) K for the Liquid Region and at Ambient Pressure
n 0 1.41826
293.15
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n 0 1.41780
293.15
Densities and derived thermodynamic properties of binary mixtures of diethylcarbonate, acetophenone, and 1-hexanol at T = (293.15 to 323.15) K for the liquid region and at ambient pressure
n 0 1.41800
293.15
ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
n 0 1.41810
293.20
Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
n 0 1.42070
293.20
Vapor Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
n 0 1.41660
298.15
Excess Molar Enthalpies of 1,2-Propanediol + Alkan-1-ols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure (81.5 kPa)
n 0 1.41590
298.15
Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
n 0 1.41570
298.15
Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
n 0 1.41620
298.15
Phase equilibria in the ternary system isobutyl alcohol + isobutyl acetate + 1-hexanol and the binary systems isobutyl alcohol + 1-hexanol, isobutyl acetate + 1-hexanol at 101.3 kPa
n 0 1.41610
298.15
Densities, Excess Molar Volumes, and Isobaric Thermal Expansibilities for 1,2-Ethanediol + 1-Butanol, or 1-Hexanol, or 1-Octanol in the Temperature Range from (293.15 to 313.15) K
n 0 1.41550
298.15
Ternary liquid liquid equilibrium data for the (water + butyric acid + n-hexane or n-hexanol) systems at T = (298.2, 308.2, and 318.2) K
n 0 1.41600
298.15
Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
n 0 1.41600
298.15
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n 0 1.41610
298.15
Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
n 0 1.41738
298.15
Atmospheric densities and interfacial tensions for 1- alkanol (1-butanol to 1-octanol) + water and ether (MTBE, ETBE, DIPE, TAME and THP) + water demixed mixtures.
n 0 1.41580
298.15
Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
n 0 1.41570
298.15
Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
n 0 1.41650
298.15
Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
n 0 1.41550
298.20
Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
n 0 1.41340
303.15
Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
n 0 1.41423
303.15
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
n 0 1.41423
303.15
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
n 0 1.41570
303.15
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n 0 1.41410
308.15
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
n 0 1.41270
313.15
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
ρl [765.64; 827.82]
kg/m3
[283.15; 363.15]
ρl 825.94
kg/m3
283.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 827.82
kg/m3
283.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 826.03
kg/m3
283.15
Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 824.25
kg/m3
288.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 822.00
kg/m3
288.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 822.26
kg/m3
288.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 822.26
kg/m3
288.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 822.42
kg/m3
288.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 819.00
kg/m3
293.00
KDB
ρl 818.90
kg/m3
293.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 818.00
kg/m3
293.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 818.70
kg/m3
293.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 819.00
kg/m3
293.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 818.69
kg/m3
293.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 818.88
kg/m3
293.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 818.70
kg/m3
293.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 818.70
kg/m3
293.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 818.75
kg/m3
293.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 820.65
kg/m3
293.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 815.16
kg/m3
298.10
Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
ρl 815.30
kg/m3
298.15
Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl 815.65
kg/m3
298.15
Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
ρl 815.21
kg/m3
298.15
Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
ρl 815.20
kg/m3
298.15
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl 815.27
kg/m3
298.15
Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
ρl 815.34
kg/m3
298.15
Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 815.50
kg/m3
298.15
Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 815.15
kg/m3
298.15
Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
ρl 815.26
kg/m3
298.15
Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
ρl 815.20
kg/m3
298.15
Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
ρl 815.19
kg/m3
298.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 815.10
kg/m3
298.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 814.94
kg/m3
298.15
Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl 815.10
kg/m3
298.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 815.11
kg/m3
298.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 815.30
kg/m3
298.15
Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl 815.31
kg/m3
298.15
FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 815.32
kg/m3
298.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 814.94
kg/m3
298.15
Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl 815.29
kg/m3
298.15
Densities, speeds of sound and viscosities of binary mixtures of tetrahydrofuran with 1-hexanol, 1-octanol and 1-decanol at T = (298.15 to 313.15) K
ρl 815.90
kg/m3
298.15
Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
ρl 815.40
kg/m3
298.15
Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
ρl 815.00
kg/m3
298.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 815.12
kg/m3
298.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 815.30
kg/m3
298.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 815.70
kg/m3
298.15
Thermodynamics of 1,3-dimethylurea in eight alcohols
ρl 814.90
kg/m3
298.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 814.95
kg/m3
298.15
Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
ρl 815.02
kg/m3
298.15
Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
ρl 817.03
kg/m3
298.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 815.17
kg/m3
298.20
Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
ρl 815.88
kg/m3
298.20
Isothermal vapor-liquid equilibria, excess molar volume and the deviation of refractive indices for binary mixtures of 1-butanol, 1- hexanol, 3-methyl-1-butanol and butyl acetate
ρl 811.50
kg/m3
303.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 812.00
kg/m3
303.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 813.39
kg/m3
303.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 811.70
kg/m3
303.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 811.52
kg/m3
303.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 811.51
kg/m3
303.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 811.39
kg/m3
303.15
Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
ρl 811.60
kg/m3
303.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 811.50
kg/m3
303.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 811.30
kg/m3
303.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 811.74
kg/m3
303.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 811.70
kg/m3
303.15
FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 807.90
kg/m3
308.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 808.00
kg/m3
308.15
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl 807.98
kg/m3
308.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 807.90
kg/m3
308.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 807.89
kg/m3
308.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 808.06
kg/m3
308.15
FT-IR studies on excess thermodynamic properties of binary liquid mixtures o-chlorotoluene with 1-propanol, 1-butanol, 1-pentanol, 1-hexanol and 1-heptanol at different temperatures
ρl 809.71
kg/m3
308.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 807.60
kg/m3
308.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 808.13
kg/m3
308.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 808.40
kg/m3
308.15
Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 807.88
kg/m3
308.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 808.10
kg/m3
308.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 804.46
kg/m3
313.15
Excess molar volumes of binary mixtures of 1,3-dimethylimidazolidin-2-one with an alkan-1-ol at the temperatures 283.15 K, 298.15 K, and 313.15 K
ρl 804.23
kg/m3
313.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 804.50
kg/m3
313.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 803.90
kg/m3
313.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 806.00
kg/m3
313.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 804.20
kg/m3
313.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 805.00
kg/m3
313.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 804.50
kg/m3
313.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 804.25
kg/m3
313.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 804.34
kg/m3
313.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 804.20
kg/m3
313.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 801.00
kg/m3
318.15
Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 800.56
kg/m3
318.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 800.60
kg/m3
318.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 802.27
kg/m3
318.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 800.66
kg/m3
318.15
Volume effects for binary mixtures of propane-1,2-diol with methanol, propan-1-ol, hexan-1-ol, octan-1-ol, or nonan-1-ol at temperatures (293.15 to 318.15) K
ρl 800.80
kg/m3
318.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 800.56
kg/m3
318.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 800.10
kg/m3
318.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 800.83
kg/m3
318.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 800.60
kg/m3
318.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 800.60
kg/m3
318.15
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl 796.85
kg/m3
323.15
Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
ρl 796.20
kg/m3
323.15
Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
ρl 796.80
kg/m3
323.15
Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
ρl 798.49
kg/m3
323.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 796.85
kg/m3
323.15
Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
ρl 796.80
kg/m3
323.15
Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
ρl 798.00
kg/m3
323.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 797.12
kg/m3
323.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 797.10
kg/m3
323.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 794.67
kg/m3
328.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 793.40
kg/m3
328.15
Density and Viscosity of Binary Liquid Mixtures of Ethanol + 1-Hexanol and Ethanol + 1-Heptanol from (293.15 to 328.15) K at 0.1 MPa
ρl 793.37
kg/m3
328.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 793.20
kg/m3
328.15
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl 793.50
kg/m3
328.15
Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 790.80
kg/m3
333.15
Volumetric properties of the boldine + alcohol mixtures at atmospheric pressure from 283.15 to 333.15K A new method for the determination of the density of pure boldine
ρl 789.57
kg/m3
333.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 791.00
kg/m3
333.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 785.50
kg/m3
338.15
Effect of temperature and composition on the density, viscosity, surface tension, and thermodynamic properties of binary mixtures of N-octylisoquinolinium bis{(trifluoromethyl)sulfonyl}imide with alcohols
ρl 785.90
kg/m3
338.15
Viscosities and Densities of Fatty Alcohol Mixtures from 298.15 to 338.15 K: Estimation by Kay's Rule and Prediction by the UNIFAC-VISCO and GC-UNIMOD Group Contribution Methods
ρl 785.72
kg/m3
338.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 783.00
kg/m3
343.15
Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
ρl 781.83
kg/m3
343.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 777.86
kg/m3
348.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 773.86
kg/m3
353.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 769.78
kg/m3
358.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
ρl 765.64
kg/m3
363.15
Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
Δfus S 68.11
J/mol×K
225.80
NIST
csound,fluid [1237.50; 1339.20]
m/s
[288.15; 318.15]
csound,fluid 1339.20
m/s
288.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1320.38
m/s
293.15
Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1321.20
m/s
293.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1320.32
m/s
293.15
Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1320.11
m/s
293.15
Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid 1303.19
m/s
298.15
Densities, Excess Molar Volumes, Ultrasonic Speeds, and Isentropic Compressibilities of Hexan-1-ol with 1,2-Dichloroethane, 1,2-Dibromoethane, and 1,1,2,2-Tetrachloroethene at (293.15 and 298.15) K
csound,fluid 1312.40
m/s
298.15
Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
csound,fluid 1306.90
m/s
298.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1303.03
m/s
298.15
Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1303.54
m/s
298.15
Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1286.68
m/s
303.15
Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1289.50
m/s
303.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1286.34
m/s
303.15
Densities, Excess Molar Volumes, Speeds of Sound at (293.15, 298.15, and 303.15) K and Isentropic Compressibilities at 298.15 K for 1-Butanol, 1-Pentanol, or 1-Hexanol + Dibutylether Systems
csound,fluid 1270.00
m/s
308.15
Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1275.70
m/s
308.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1256.30
m/s
313.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
csound,fluid 1253.54
m/s
313.15
Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
csound,fluid 1237.50
m/s
318.15
Ultrasonic study of molecular interactions in binary mixtures of methyl acrylate with 1-alkanols (C4 to C10) at temperatures from (288.15 to 318.15) K
γ [0.02; 0.03]
N/m
[288.15; 328.15]
γ 0.03
N/m
288.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.03
N/m
288.15
Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.03
N/m
288.15
Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ 0.03
N/m
288.15
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03
N/m
293.15
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03
N/m
293.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.03
N/m
298.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.03
N/m
298.15
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03
N/m
298.15
Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.03
N/m
298.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02
N/m
298.15
Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ 0.03
N/m
298.20
KDB
γ 0.02
N/m
303.15
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.03
N/m
303.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02
N/m
303.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02
N/m
308.15
Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
γ 0.02
N/m
308.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02
N/m
308.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02
N/m
308.15
Density and surface tension variation with temperature for n-nonane + 1-hexanol
γ 0.02
N/m
308.15
Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ 0.02
N/m
313.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02
N/m
313.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02
N/m
318.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02
N/m
318.15
The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
γ 0.02
N/m
318.15
Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
γ 0.02
N/m
323.15
Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
γ 0.02
N/m
328.15
Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
