| Property |
Value |
Unit |
Temperature (K) |
Source |
| 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
|
| ΔfusH |
[15.38; 15.48] |
kJ/mol |
[225.80; 225.80] |
|
| ΔfusH |
15.38 |
kJ/mol |
225.80 |
NIST
|
| ΔfusH |
15.48 |
kJ/mol |
225.80 |
NIST
|
| ΔfusH |
15.48 |
kJ/mol |
225.80 |
NIST
|
| ΔvapH |
[44.50; 62.00] |
kJ/mol |
[295.50; 430.50] |
|
|
|
| ΔvapH |
61.20 |
kJ/mol |
295.50 |
NIST
|
| ΔvapH |
62.00 |
kJ/mol |
296.50 |
NIST
|
| ΔvapH |
61.90 ± 0.20 |
kJ/mol |
300.50 |
NIST
|
| ΔvapH |
57.70 |
kJ/mol |
320.50 |
NIST
|
| ΔvapH |
58.50 ± 0.20 |
kJ/mol |
328.00 |
NIST
|
| ΔvapH |
57.60 ± 0.20 |
kJ/mol |
343.00 |
NIST
|
| ΔvapH |
56.00 |
kJ/mol |
357.50 |
NIST
|
| ΔvapH |
55.20 ± 0.20 |
kJ/mol |
358.00 |
NIST
|
| ΔvapH |
59.70 |
kJ/mol |
364.00 |
NIST
|
| ΔvapH |
53.80 ± 0.20 |
kJ/mol |
368.00 |
NIST
|
| ΔvapH |
57.90 |
kJ/mol |
369.00 |
NIST
|
| ΔvapH |
58.50 |
kJ/mol |
378.00 |
NIST
|
| ΔvapH |
57.90 |
kJ/mol |
379.00 |
NIST
|
| ΔvapH |
51.40 |
kJ/mol |
393.00 |
NIST
|
| ΔvapH |
47.90 |
kJ/mol |
398.50 |
NIST
|
| ΔvapH |
48.53 |
kJ/mol |
430.30 |
KDB
|
| ΔvapH |
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
|
| n0 |
[1.41270; 1.42070] |
|
[293.10; 313.15] |
|
|
|
| n0 |
1.41800 |
|
293.10 |
Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
|
| n0 |
1.41750 |
|
293.15 |
Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
|
| n0 |
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
|
| n0 |
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
|
| n0 |
1.41807 |
|
293.15 |
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
|
| n0 |
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
|
| n0 |
1.41826 |
|
293.15 |
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
|
| n0 |
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
|
| n0 |
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
|
| n0 |
1.41810 |
|
293.20 |
Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
|
| n0 |
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
|
| n0 |
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)
|
| n0 |
1.41590 |
|
298.15 |
Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
|
| n0 |
1.41570 |
|
298.15 |
Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
|
| n0 |
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
|
| n0 |
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
|
| n0 |
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
|
| n0 |
1.41600 |
|
298.15 |
Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
|
| n0 |
1.41600 |
|
298.15 |
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
|
| n0 |
1.41610 |
|
298.15 |
Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
|
| n0 |
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.
|
| n0 |
1.41580 |
|
298.15 |
Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
|
| n0 |
1.41570 |
|
298.15 |
Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
|
| n0 |
1.41650 |
|
298.15 |
Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
|
| n0 |
1.41550 |
|
298.20 |
Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
|
| n0 |
1.41340 |
|
303.15 |
Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
|
| n0 |
1.41423 |
|
303.15 |
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
|
| n0 |
1.41423 |
|
303.15 |
Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
|
| n0 |
1.41570 |
|
303.15 |
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
|
| n0 |
1.41410 |
|
308.15 |
Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
|
| n0 |
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
|
| ΔfusS |
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
|
