- InChI
- InChI=1S/C6H14O/c1-2-3-4-5-6-7/h7H,2-6H2,1H3
- InChI Key
- ZSIAUFGUXNUGDI-UHFFFAOYSA-N
- Formula
- C6H14O
- SMILES
- CCCCCCO
- Molecular Weight1
- 102.17
- CAS
- 111-27-3
- Other Names
-
- 1-Hexyl alcohol
- 1-Hydroxyhexane
- Amylcarbinol
- Caproyl alcohol
- Epal 6
- Hexan-1-ol
- Hexanol
- Hexanol-(1)
- Hexyl alcohol
- NSC 9254
- Pentylcarbinol
- n-C6H13OH
- n-Hexan-1-ol
- n-Hexanol
- n-Hexyl alcohol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5600 | KDB | |
| PAff | 799.00 | kJ/mol | NIST |
| Tig | 577.59 | K | KDB |
| ΔcH°liquid | [-3984.37; -3978.10] | kJ/mol |
|
| ΔcH°liquid | -3984.37 ± 0.44 | kJ/mol | NIST |
| ΔcH°liquid | -3982.60 ± 0.92 | kJ/mol | NIST |
| ΔcH°liquid | -3978.10 ± 2.00 | kJ/mol | NIST |
| ΔcH°liquid | -3978.10 | kJ/mol | NIST |
| μ | 1.80 | debye | KDB |
| η | [0.0044395; 0.0052910] | Pa×s |
|
| η | 0.0052910 | Pa×s | Studies... |
| η | 0.0044395 | Pa×s | Volumet... |
| LFL | 1.20 | % in Air | KDB |
| UFL | 7.70 | % in Air | KDB |
| Tflash,cc | 338.15 | K | KDB |
| Tflash,oc | 335.93 | K | KDB |
| ΔfG° | -135.70 | kJ/mol | KDB |
| ΔfH°gas | -317.80 | kJ/mol | KDB |
| ΔfH°liquid | [-387.70; -377.50] | kJ/mol |
|
| ΔfH°liquid | -377.50 ± 0.44 | kJ/mol | NIST |
| ΔfH°liquid | -379.40 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -383.90 ± 2.00 | kJ/mol | NIST |
| ΔfH°liquid | -387.70 | kJ/mol | NIST |
| ΔfusH° | 16.73 | kJ/mol | Heat Ca... |
| ΔvapH° | [59.10; 69.20] | kJ/mol |
|
| ΔvapH° | 61.61 | kJ/mol | NIST |
| ΔvapH° | 59.10 | kJ/mol | NIST |
| ΔvapH° | 59.90 | kJ/mol | NIST |
| ΔvapH° | 61.70 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 61.10 | kJ/mol | NIST |
| ΔvapH° | 62.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 61.50 | kJ/mol | NIST |
| ΔvapH° | 61.60 | kJ/mol | NIST |
| ΔvapH° | 61.85 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 60.80 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 61.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 61.60 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 62.80 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | Outlier 69.20 | kJ/mol | NIST |
| IE | [9.89; 10.35] | eV |
|
| IE | 9.89 | eV | NIST |
| IE | 10.35 | eV | NIST |
| log10WS | [-1.24; -1.24] |
|
|
| log10WS | -1.24 | Aq. Sol... | |
| log10WS | -1.24 | Estimat... | |
| logPoct/wat | 1.559 | Crippen Calculated Property | |
| McVol | 101.270 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [3413.00; 3420.00] | kPa |
|
| Pc | 3417.00 | kPa | KDB |
| Pc | 3420.00 ± 20.00 | kPa | NIST |
| Pc | 3420.00 ± 50.00 | kPa | NIST |
| Pc | 3413.00 ± 6.00 | kPa | NIST |
| Pc | 3413.00 ± 20.00 | kPa | NIST |
| ρc | [259.52; 267.70] | kg/m3 |
|
| ρc | 263.61 ± 2.04 | kg/m3 | NIST |
| ρc | 267.70 | kg/m3 | NIST |
| ρc | 259.52 ± 6.13 | kg/m3 | NIST |
| ρc | 267.70 ± 3.07 | kg/m3 | NIST |
| Inp | [136.97; 896.80] |
|
|
| Inp | 889.40 | NIST | |
| Inp | 896.80 | NIST | |
| Inp | 870.10 | NIST | |
| Inp | 866.30 | NIST | |
| Inp | 862.30 | NIST | |
| Inp | 861.10 | NIST | |
| Inp | 859.90 | NIST | |
| Inp | 859.54 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 848.20 | NIST | |
| Inp | 831.90 | NIST | |
| Inp | 836.60 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 879.50 | NIST | |
| Inp | 822.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 823.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 831.20 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 847.90 | NIST | |
| Inp | 865.10 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 852.70 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 865.60 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 828.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 878.10 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 832.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 859.11 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 827.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 865.80 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | Outlier 136.97 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 865.10 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 852.70 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | Outlier 136.97 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 862.00 | NIST | |
| I | [1308.00; 1398.00] |
|
|
| I | 1384.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1378.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1347.99 | NIST | |
| I | 1346.20 | NIST | |
| I | 1344.79 | NIST | |
| I | 1348.98 | NIST | |
| I | Outlier 1315.00 | NIST | |
| I | 1329.00 | NIST | |
| I | 1326.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1350.00 | NIST | |
| I | Outlier 1321.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1347.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1339.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1376.00 | NIST | |
| I | 1356.00 | NIST | |
| I | Outlier 1308.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1337.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1340.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1343.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1344.00 | NIST | |
| I | Outlier 1320.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1367.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1344.00 | NIST | |
| I | Outlier 1320.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1354.00 | NIST | |
| I | Outlier 1396.00 | NIST | |
| I | 1343.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1360.60 | NIST | |
| I | 1343.00 | NIST | |
| I | 1358.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1368.00 | NIST | |
| I | Outlier 1315.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1333.00 | NIST | |
| I | 1335.00 | NIST | |
| I | 1349.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1367.00 | NIST | |
| I | 1364.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1343.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1337.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1343.00 | NIST | |
| I | Outlier 1318.00 | NIST | |
| I | Outlier 1314.00 | NIST | |
| I | 1324.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1372.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1370.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1342.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1368.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1360.00 | NIST | |
| I | Outlier 1387.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1360.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1352.00 | NIST | |
| I | Outlier 1321.00 | NIST | |
| I | 1378.00 | NIST | |
| I | 1367.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1346.00 | NIST | |
| I | Outlier 1311.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1379.00 | NIST | |
| I | Outlier 1398.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1349.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1359.00 | NIST | |
| I | Outlier 1320.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1354.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1354.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1369.00 | NIST | |
| I | 1374.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1341.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1365.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1360.00 | NIST | |
| I | Outlier 1320.00 | NIST | |
| I | 1380.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1365.40 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1349.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1361.00 | NIST | |
| I | Outlier 1321.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1371.00 | NIST | |
| I | 1375.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1361.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1340.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1359.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1352.00 | NIST | |
| I | 1336.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1345.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1331.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1356.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1346.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1372.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1368.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1343.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1362.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1373.00 | NIST | |
| I | 1360.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1365.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1328.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1341.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1365.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1330.00 | NIST | |
| I | 1347.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1372.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1367.00 | NIST | |
| I | 1352.00 | NIST | |
| I | Outlier 1316.00 | NIST | |
| I | 1360.00 | NIST | |
| I | 1351.00 | NIST | |
| I | 1345.00 | NIST | |
| I | 1339.00 | NIST | |
| I | 1363.00 | NIST | |
| I | 1371.00 | NIST | |
| I | Outlier 1396.00 | NIST | |
| I | 1358.00 | NIST | |
| I | 1356.00 | NIST | |
| I | 1368.00 | NIST | |
| I | 1353.00 | NIST | |
| I | 1349.00 | NIST | |
| I | 1338.00 | NIST | |
| I | 1325.00 | NIST | |
| I | 1336.00 | NIST | |
| I | 1357.00 | NIST | |
| I | 1359.00 | NIST | |
| I | 1362.00 | NIST | |
| I | 1355.00 | NIST | |
| I | 1366.00 | NIST | |
| I | 1352.00 | NIST | |
| I | Outlier 1392.00 | NIST | |
| I | 1350.00 | NIST | |
| I | 1365.00 | NIST | |
| I | 1354.00 | NIST | |
| I | 1344.00 | NIST | |
| I | 1332.00 | NIST | |
| I | 1375.00 | NIST | |
| I | 1378.00 | NIST | |
| I | 1379.00 | NIST | |
| I | 1386.00 | NIST | |
| I | 1348.00 | NIST | |
| I | 1380.00 | NIST | |
| I | 1384.00 | NIST | |
| I | 1344.79 | NIST | |
| I | 1342.00 | NIST | |
| S°gas | 439.70 ± 2.10 | J/mol×K | NIST |
| S°liquid | 287.40 | J/mol×K | NIST |
| Tboil | [409.15; 440.15] | K |
|
| Tboil | 430.70 | K | KDB |
| Tboil | 430.75 | K | Excess ... |
| Tboil | 430.50 | K | Phase e... |
| Tboil | 430.11 | K | Vapor-l... |
| Tboil | 429.70 | K | NIST |
| Tboil | 431.20 | K | NIST |
| Tboil | 430.50 | K | NIST |
| Tboil | 430.00 ± 0.12 | K | NIST |
| Tboil | 430.50 ± 0.50 | K | NIST |
| Tboil | 430.40 ± 0.30 | K | NIST |
| Tboil | 430.25 | K | NIST |
| Tboil | 430.55 ± 0.50 | K | NIST |
| Tboil | 430.65 ± 0.70 | K | NIST |
| Tboil | 429.40 ± 0.70 | K | NIST |
| Tboil | 428.15 ± 1.00 | K | NIST |
| Tboil | 430.25 | K | NIST |
| Tboil | 428.15 ± 1.00 | K | NIST |
| Tboil | 427.65 ± 3.00 | K | NIST |
| Tboil | 430.15 ± 2.00 | K | NIST |
| Tboil | 429.65 ± 2.00 | K | NIST |
| Tboil | 431.15 ± 2.00 | K | NIST |
| Tboil | 426.65 ± 2.00 | K | NIST |
| Tboil | 430.55 ± 0.30 | K | NIST |
| Tboil | 426.90 ± 2.00 | K | NIST |
| Tboil | 430.45 ± 0.50 | K | NIST |
| Tboil | 428.65 ± 1.50 | K | NIST |
| Tboil | 430.27 ± 0.20 | K | NIST |
| Tboil | 429.65 ± 1.00 | K | NIST |
| Tboil | 430.95 ± 0.70 | K | NIST |
| Tboil | 429.65 ± 2.00 | K | NIST |
| Tboil | 425.65 ± 3.00 | K | NIST |
| Tboil | 429.75 ± 0.70 | K | NIST |
| Tboil | 430.15 ± 0.70 | K | NIST |
| Tboil | 428.90 ± 0.70 | K | NIST |
| Tboil | 429.90 ± 1.00 | K | NIST |
| Tboil | 428.65 ± 2.00 | K | NIST |
| Tboil | 430.65 ± 1.00 | K | NIST |
| Tboil | 431.05 ± 0.50 | K | NIST |
| Tboil | 428.65 ± 2.00 | K | NIST |
| Tboil | 428.45 ± 2.00 | K | NIST |
| Tboil | 429.60 ± 0.70 | K | NIST |
| Tboil | 430.55 ± 1.00 | K | NIST |
| Tboil | 430.62 ± 0.20 | K | NIST |
| Tboil | 428.85 ± 0.30 | K | NIST |
| Tboil | Outlier 421.15 ± 2.00 | K | NIST |
| Tboil | 429.65 ± 0.50 | K | NIST |
| Tboil | 431.00 ± 0.30 | K | NIST |
| Tboil | 430.20 ± 0.50 | K | NIST |
| Tboil | 430.95 ± 0.50 | K | NIST |
| Tboil | 430.80 ± 0.30 | K | NIST |
| Tboil | 432.15 ± 2.00 | K | NIST |
| Tboil | 430.15 ± 0.70 | K | NIST |
| Tboil | 429.00 ± 0.40 | K | NIST |
| Tboil | Outlier 440.15 ± 5.00 | K | NIST |
| Tboil | 431.15 ± 2.00 | K | NIST |
| Tboil | Outlier 409.15 ± 3.00 | K | NIST |
| Tboil | 428.15 ± 2.00 | K | NIST |
| Tboil | 428.70 ± 0.70 | K | NIST |
| Tboil | 430.15 ± 3.00 | K | NIST |
| Tboil | 429.00 ± 3.00 | K | NIST |
| Tboil | 429.75 ± 1.00 | K | NIST |
| Tboil | 430.60 ± 1.00 | K | NIST |
| Tboil | 430.45 ± 2.00 | K | NIST |
| Tboil | 423.15 ± 4.00 | K | NIST |
| Tc | 610.30 | K | KDB |
| Tfus | [224.75; 229.00] | K |
|
| Tfus | 224.75 | K | Aq. Sol... |
| Tfus | 228.50 | K | KDB |
| Tfus | 229.00 | K | Vapour ... |
| Ttriple | 225.80 ± 0.30 | K | NIST |
| Vc | [0.387; 0.387] | m3/kmol |
|
| Vc | 0.387 | m3/kmol | KDB |
| Vc | 0.387 | m3/kmol | NIST |
| Zc | 0.2606010 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [207.67; 259.79] | J/mol×K | [428.86; 589.96] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 210 220 230 240 250 260 450 500 550 | ||||
| Cp,gas | 207.67 | J/mol×K | 428.86 | Joback Calculated Property |
| Cp,gas | 217.18 | J/mol×K | 455.71 | Joback Calculated Property |
| Cp,gas | 226.36 | J/mol×K | 482.56 | Joback Calculated Property |
| Cp,gas | 235.20 | J/mol×K | 509.41 | Joback Calculated Property |
| Cp,gas | 243.71 | J/mol×K | 536.26 | Joback Calculated Property |
| Cp,gas | 251.90 | J/mol×K | 563.11 | Joback Calculated Property |
| Cp,gas | 259.79 | J/mol×K | 589.96 | Joback Calculated Property |
| Cp,liquid | [232.46; 249.15] | J/mol×K | [290.01; 303.74] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 235 240 245 250 290 295 300 | ||||
| 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 | 243.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 239.68 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 239.62 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 240.57 | 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 | 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 300 320 340 | ||||
| η | 0.0074590 | Pa×s | 283.15 | Densiti... |
| η | 0.0053350 | Pa×s | 293.15 | Densiti... |
| η | 0.0054120 | Pa×s | 293.15 | A Study... |
| η | 0.0046426 | Pa×s | 298.15 | Densiti... |
| η | 0.0045940 | Pa×s | 298.15 | Acousti... |
| η | 0.0046050 | Pa×s | 298.15 | Densiti... |
| η | 0.0045960 | Pa×s | 298.15 | A Study... |
| η | 0.0039985 | Pa×s | 303.15 | Densiti... |
| η | 0.0038290 | Pa×s | 303.15 | Volumet... |
| η | 0.0039640 | Pa×s | 303.15 | A Study... |
| η | 0.0039170 | Pa×s | 303.15 | Densiti... |
| η | 0.0039440 | Pa×s | 303.15 | Densiti... |
| η | 0.0037630 | Pa×s | 303.15 | Densiti... |
| η | 0.0038870 | Pa×s | 303.15 | Acousti... |
| η | 0.0038290 | Pa×s | 303.15 | Thermod... |
| η | 0.0033180 | Pa×s | 308.15 | Density... |
| η | 0.0034140 | Pa×s | 308.15 | Densiti... |
| η | 0.0033590 | Pa×s | 308.15 | Acousti... |
| η | 0.0034713 | Pa×s | 308.15 | Densiti... |
| η | 0.0029660 | Pa×s | 313.15 | A Study... |
| η | 0.0029600 | Pa×s | 313.15 | Densiti... |
| η | 0.0029140 | Pa×s | 313.15 | Acousti... |
| η | 0.0029370 | Pa×s | 313.15 | Densiti... |
| η | 0.0028790 | Pa×s | 313.15 | Thermod... |
| η | 0.0028790 | Pa×s | 313.15 | Volumet... |
| η | 0.0025180 | Pa×s | 318.15 | Density... |
| η | 0.0025810 | Pa×s | 318.15 | Densiti... |
| η | 0.0022510 | Pa×s | 323.15 | Densiti... |
| η | 0.0022760 | Pa×s | 323.15 | Densiti... |
| η | 0.0021720 | Pa×s | 323.15 | Densiti... |
| η | 0.0022150 | Pa×s | 323.15 | Thermod... |
| η | 0.0022150 | Pa×s | 323.15 | Volumet... |
| η | 0.0016540 | Pa×s | 333.15 | Densiti... |
| η | 0.0014110 | Pa×s | 343.15 | Densiti... |
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 45 50 55 60 300 350 400 | ||||
| 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 | Densiti... |
| ν | 0.0000036 | m2/s | 313.15 | Densiti... |
| Pvap | [1.43e-04; 106.98] | kPa | [237.95; 432.32] |
|
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 250 300 350 400 | ||||
| Pvap | 1.43e-04 | kPa | 237.95 | Vapor p... |
| Pvap | 1.45e-04 | kPa | 238.00 | Vapor p... |
| Pvap | 1.43e-04 | kPa | 238.00 | Vapor p... |
| Pvap | 2.96e-04 | kPa | 243.20 | Vapor p... |
| Pvap | 2.96e-04 | kPa | 243.20 | Vapor p... |
| Pvap | 2.93e-04 | kPa | 243.25 | Vapor p... |
| Pvap | 5.64e-04 | kPa | 248.20 | Vapor p... |
| Pvap | 5.60e-04 | kPa | 248.20 | Vapor p... |
| Pvap | 5.69e-04 | kPa | 248.20 | Vapor p... |
| Pvap | 1.06e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 1.05e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 1.05e-03 | kPa | 253.15 | Vapor p... |
| Pvap | 1.92e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 1.92e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 1.92e-03 | kPa | 258.15 | Vapor p... |
| Pvap | 3.39e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 3.38e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 3.39e-03 | kPa | 263.15 | Vapor p... |
| Pvap | 4.68e-03 | kPa | 265.00 | Measure... |
| Pvap | 5.84e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 5.84e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 5.84e-03 | kPa | 268.15 | Vapor p... |
| Pvap | 6.64e-03 | kPa | 268.20 | Measure... |
| Pvap | 9.86e-03 | kPa | 273.15 | Vapor p... |
| Pvap | 9.87e-03 | kPa | 273.15 | Vapor p... |
| Pvap | 9.87e-03 | kPa | 273.15 | Vapor p... |
| Pvap | 0.01 | kPa | 273.40 | Measure... |
| Pvap | 0.01 | kPa | 273.65 | Vapor p... |
| Pvap | 0.01 | kPa | 273.65 | Vapor p... |
| Pvap | 0.01 | kPa | 273.65 | Vapor p... |
| Pvap | 0.02 | kPa | 278.15 | Vapor p... |
| Pvap | 0.02 | kPa | 278.15 | Vapor p... |
| Pvap | 0.02 | kPa | 278.15 | Vapor p... |
| Pvap | 0.02 | kPa | 278.20 | Measure... |
| Pvap | 0.03 | kPa | 283.15 | Vapor p... |
| Pvap | 0.03 | kPa | 283.15 | Vapor p... |
| Pvap | 0.03 | kPa | 283.15 | Vapor p... |
| Pvap | 0.03 | kPa | 283.20 | Measure... |
| Pvap | 0.05 | kPa | 288.10 | Measure... |
| Pvap | 0.04 | kPa | 288.15 | Vapor p... |
| Pvap | 0.04 | kPa | 288.15 | Vapor p... |
| Pvap | 0.04 | kPa | 288.15 | Vapor p... |
| Pvap | 0.07 | kPa | 293.15 | Vapor p... |
| Pvap | 0.07 | kPa | 293.15 | Vapor p... |
| Pvap | 0.07 | kPa | 293.15 | Vapor p... |
| Pvap | 0.07 | kPa | 293.20 | Measure... |
| Pvap | 0.07 | kPa | 293.30 | Measure... |
| Pvap | 0.10 | kPa | 298.15 | Vapor p... |
| Pvap | 0.10 | kPa | 298.15 | Vapor p... |
| Pvap | 0.12 | kPa | 298.15 | Vapor P... |
| Pvap | 0.10 | kPa | 298.15 | Vapor p... |
| Pvap | 0.12 | kPa | 298.20 | Measure... |
| Pvap | 0.11 | kPa | 298.30 | Measure... |
| Pvap | 0.17 | kPa | 303.15 | Vapor P... |
| Pvap | 0.15 | kPa | 303.15 | Vapor p... |
| Pvap | 0.15 | kPa | 303.15 | Vapor p... |
| Pvap | 0.15 | kPa | 303.15 | Vapor p... |
| Pvap | 0.17 | kPa | 303.20 | Measure... |
| Pvap | 0.17 | kPa | 303.20 | Measure... |
| Pvap | 0.17 | kPa | 303.30 | Measure... |
| Pvap | 0.25 | kPa | 308.15 | Vapor P... |
| Pvap | 0.22 | kPa | 308.15 | Vapor p... |
| Pvap | 0.22 | kPa | 308.15 | Vapor p... |
| Pvap | 0.22 | kPa | 308.15 | Vapor p... |
| Pvap | 0.25 | kPa | 308.20 | Measure... |
| Pvap | 0.25 | kPa | 308.30 | Measure... |
| Pvap | 0.30 | kPa | 310.40 | Measure... |
| Pvap | 0.36 | kPa | 313.10 | Measure... |
| Pvap | 0.36 | kPa | 313.15 | Vapor P... |
| Pvap | 0.37 | kPa | 313.20 | Measure... |
| Pvap | 0.52 | kPa | 318.15 | Vapor P... |
| Pvap | 0.53 | kPa | 318.20 | Measure... |
| Pvap | 0.53 | kPa | 318.20 | Measure... |
| Pvap | 0.73 | kPa | 323.15 | Vapor P... |
| Pvap | 0.71 | kPa | 323.20 | Measure... |
| Pvap | 0.75 | kPa | 323.20 | Measure... |
| Pvap | 1.03 | kPa | 328.10 | Measure... |
| Pvap | 1.01 | kPa | 328.15 | Vapor P... |
| Pvap | 1.01 | kPa | 328.20 | Measure... |
| Pvap | 1.43 | kPa | 333.10 | Measure... |
| Pvap | 1.40 | kPa | 333.15 | Vapor P... |
| Pvap | 1.46 | kPa | 333.20 | Measure... |
| Pvap | 1.90 | kPa | 338.15 | Vapor P... |
| Pvap | 1.98 | kPa | 338.20 | Measure... |
| Pvap | 2.54 | kPa | 343.15 | Vapor P... |
| Pvap | 2.64 | kPa | 343.20 | Measure... |
| Pvap | 2.04 | kPa | 343.46 | Vapor-L... |
| Pvap | 2.16 | kPa | 344.20 | Vapor-L... |
| Pvap | 2.23 | kPa | 344.60 | Vapor-L... |
| Pvap | 2.35 | kPa | 345.36 | Vapor-L... |
| Pvap | 2.47 | kPa | 346.17 | Vapor-L... |
| Pvap | 2.67 | kPa | 347.27 | Vapor-L... |
| Pvap | 2.79 | kPa | 348.10 | Vapor-L... |
| Pvap | 3.38 | kPa | 348.15 | Vapor P... |
| Pvap | 3.48 | kPa | 348.20 | Measure... |
| Pvap | 2.85 | kPa | 348.35 | Vapor-L... |
| Pvap | 3.04 | kPa | 349.38 | Vapor-L... |
| Pvap | 3.11 | kPa | 349.75 | Vapor-L... |
| Pvap | 3.32 | kPa | 350.75 | Vapor-L... |
| Pvap | 3.44 | kPa | 351.39 | Vapor-L... |
| Pvap | 3.64 | kPa | 352.20 | Vapor-L... |
| Pvap | 3.73 | kPa | 352.63 | Vapor-L... |
| Pvap | 3.83 | kPa | 353.00 | Vapor-L... |
| Pvap | 4.43 | kPa | 353.15 | Vapor P... |
| Pvap | 4.64 | kPa | 353.20 | Measure... |
| Pvap | 3.89 | kPa | 353.31 | Vapor-L... |
| Pvap | 3.96 | kPa | 353.82 | Vapor-L... |
| Pvap | 4.31 | kPa | 355.20 | Vapor-L... |
| Pvap | 4.79 | kPa | 357.01 | Vapor-L... |
| Pvap | 5.79 | kPa | 357.20 | Measure... |
| Pvap | 5.76 | kPa | 358.15 | Vapor P... |
| Pvap | 6.13 | kPa | 358.20 | Measure... |
| Pvap | 5.15 | kPa | 358.22 | Vapor-L... |
| Pvap | 5.51 | kPa | 359.43 | Vapor-L... |
| Pvap | 5.79 | kPa | 360.34 | Vapor-L... |
| Pvap | 6.04 | kPa | 361.12 | Vapor-L... |
| Pvap | 6.29 | kPa | 361.86 | Vapor-L... |
| Pvap | 7.41 | kPa | 363.15 | Vapor P... |
| Pvap | 7.87 | kPa | 363.20 | Measure... |
| Pvap | 6.99 | kPa | 363.85 | Vapor-L... |
| Pvap | 7.27 | kPa | 364.61 | Vapor-L... |
| Pvap | 7.64 | kPa | 365.58 | Vapor-L... |
| Pvap | 7.92 | kPa | 366.30 | Vapor-L... |
| Pvap | 8.32 | kPa | 366.67 | Vapor p... |
| Pvap | 8.40 | kPa | 367.44 | Vapor-L... |
| Pvap | 8.67 | kPa | 368.05 | Vapor-L... |
| Pvap | 9.44 | kPa | 368.15 | Vapor P... |
| Pvap | 9.08 | kPa | 368.99 | Vapor-L... |
| Pvap | 9.40 | kPa | 369.67 | Vapor-L... |
| Pvap | 9.67 | kPa | 370.24 | Vapor-L... |
| Pvap | 9.95 | kPa | 370.83 | Vapor-L... |
| Pvap | 10.27 | kPa | 371.45 | Vapor-L... |
| Pvap | 10.59 | kPa | 372.10 | Vapor-L... |
| Pvap | 11.06 | kPa | 372.64 | Vapor p... |
| Pvap | 11.05 | kPa | 373.00 | Vapor-L... |
| Pvap | 11.91 | kPa | 373.15 | Vapor P... |
| Pvap | 11.43 | kPa | 373.67 | Vapor-L... |
| Pvap | 11.73 | kPa | 374.19 | Vapor-L... |
| Pvap | 12.27 | kPa | 375.14 | Vapor-L... |
| Pvap | 12.73 | kPa | 375.93 | Vapor-L... |
| Pvap | 13.15 | kPa | 376.59 | Vapor-L... |
| Pvap | 13.53 | kPa | 377.22 | Vapor-L... |
| Pvap | 13.87 | kPa | 377.56 | Vapor p... |
| Pvap | 13.71 | kPa | 377.83 | Vapor-L... |
| Pvap | 13.85 | kPa | 378.01 | Vapor-L... |
| Pvap | 14.90 | kPa | 378.15 | Vapor P... |
| Pvap | 14.15 | kPa | 378.37 | Vapor-L... |
| Pvap | 14.40 | kPa | 378.72 | Vapor-L... |
| Pvap | 14.65 | kPa | 379.10 | Vapor-L... |
| Pvap | 14.91 | kPa | 379.46 | Vapor-L... |
| Pvap | 15.12 | kPa | 379.75 | Vapor-L... |
| Pvap | 15.37 | kPa | 380.06 | Vapor-L... |
| Pvap | 15.61 | kPa | 380.41 | Vapor-L... |
| Pvap | 15.95 | kPa | 380.87 | Vapor-L... |
| Pvap | 16.15 | kPa | 381.15 | Vapor-L... |
| Pvap | 16.37 | kPa | 381.45 | Vapor-L... |
| Pvap | 16.77 | kPa | 381.80 | Vapor p... |
| Pvap | 16.77 | kPa | 381.81 | Vapor p... |
| Pvap | 16.71 | kPa | 381.89 | Vapor-L... |
| Pvap | 16.97 | kPa | 382.25 | Vapor-L... |
| Pvap | 17.21 | kPa | 382.56 | Vapor-L... |
| Pvap | 17.44 | kPa | 382.85 | Vapor-L... |
| Pvap | 18.50 | kPa | 383.15 | Vapor P... |
| Pvap | 17.69 | kPa | 383.18 | Vapor-L... |
| Pvap | 17.84 | kPa | 383.34 | Vapor-L... |
| Pvap | 18.09 | kPa | 383.67 | Vapor-L... |
| Pvap | 18.43 | kPa | 384.08 | Vapor-L... |
| Pvap | 19.05 | kPa | 384.87 | Vapor-L... |
| Pvap | 19.47 | kPa | 385.37 | Vapor-L... |
| Pvap | 19.91 | kPa | 385.86 | Vapor-L... |
| Pvap | 20.26 | kPa | 386.17 | Vapor p... |
| Pvap | 20.31 | kPa | 386.31 | Vapor-L... |
| Pvap | 20.79 | kPa | 386.83 | Vapor-L... |
| Pvap | 21.15 | kPa | 387.23 | Vapor-L... |
| Pvap | 21.48 | kPa | 387.62 | Vapor-L... |
| Pvap | 21.91 | kPa | 388.10 | Vapor-L... |
| Pvap | 22.79 | kPa | 388.15 | Vapor P... |
| Pvap | 22.37 | kPa | 388.59 | Vapor-L... |
| Pvap | 22.79 | kPa | 389.05 | Vapor-L... |
| Pvap | 23.20 | kPa | 389.48 | Vapor-L... |
| Pvap | 23.60 | kPa | 389.89 | Vapor-L... |
| Pvap | 23.95 | kPa | 390.23 | Vapor-L... |
| Pvap | 24.36 | kPa | 390.65 | Vapor-L... |
| Pvap | 24.54 | kPa | 390.77 | Vapor p... |
| Pvap | 24.54 | kPa | 390.78 | Vapor p... |
| Pvap | 24.67 | kPa | 390.93 | Vapor-L... |
| Pvap | 25.00 | kPa | 391.07 | Phase E... |
| Pvap | 25.13 | kPa | 391.40 | Vapor-L... |
| Pvap | 25.51 | kPa | 391.75 | Vapor-L... |
| Pvap | 25.83 | kPa | 392.06 | Vapor-L... |
| Pvap | 26.31 | kPa | 392.51 | Vapor-L... |
| Pvap | 26.59 | kPa | 392.77 | Vapor-L... |
| Pvap | 27.00 | kPa | 393.14 | Vapor-L... |
| Pvap | 27.86 | kPa | 393.15 | Vapor P... |
| Pvap | 29.35 | kPa | 395.23 | Vapor p... |
| Pvap | 29.35 | kPa | 395.23 | Vapor p... |
| Pvap | 30.00 | kPa | 395.62 | Phase E... |
| Pvap | 33.84 | kPa | 398.15 | Vapor P... |
| Pvap | 34.77 | kPa | 399.57 | Vapor p... |
| Pvap | 35.00 | kPa | 399.65 | Phase E... |
| Pvap | 40.00 | kPa | 402.36 | Low-Pre... |
| Pvap | 40.85 | kPa | 403.15 | Vapor P... |
| Pvap | 40.00 | kPa | 403.15 | Phase E... |
| Pvap | 40.02 | kPa | 403.66 | Low-Pre... |
| Pvap | 40.70 | kPa | 403.73 | Vapor p... |
| Pvap | 45.00 | kPa | 406.36 | Phase E... |
| Pvap | 48.72 | kPa | 407.89 | Low-Pre... |
| Pvap | 47.57 | kPa | 407.98 | Vapor p... |
| Pvap | 49.02 | kPa | 408.15 | Vapor P... |
| Pvap | 50.00 | kPa | 409.25 | Phase E... |
| Pvap | 55.00 | kPa | 411.92 | Phase E... |
| Pvap | 58.50 | kPa | 413.15 | Vapor P... |
| Pvap | 58.84 | kPa | 413.31 | Low-Pre... |
| Pvap | 60.00 | kPa | 414.44 | Phase E... |
| Pvap | 60.20 | kPa | 414.61 | Vapor p... |
| Pvap | 65.00 | kPa | 416.75 | Phase E... |
| Pvap | 69.49 | kPa | 418.15 | Vapor P... |
| Pvap | 69.27 | kPa | 418.35 | Low-Pre... |
| Pvap | 70.00 | kPa | 418.98 | Phase E... |
| Pvap | 74.69 | kPa | 420.99 | Vapor p... |
| Pvap | 75.00 | kPa | 421.05 | Phase E... |
| Pvap | 77.40 | kPa | 421.90 | Low-Pre... |
| Pvap | 80.00 | kPa | 423.01 | Phase E... |
| Pvap | 82.16 | kPa | 423.15 | Vapor P... |
| Pvap | 85.00 | kPa | 424.87 | Phase E... |
| Pvap | 85.63 | kPa | 425.15 | Low-Pre... |
| Pvap | 90.00 | kPa | 426.69 | Phase E... |
| Pvap | 92.07 | kPa | 427.54 | Low-Pre... |
| Pvap | 93.19 | kPa | 427.85 | Vapor p... |
| Pvap | 93.26 | kPa | 427.90 | Vapor p... |
| Pvap | 99.78 | kPa | 429.19 | Low-Pre... |
| Pvap | 98.12 | kPa | 429.52 | Vapor p... |
| Pvap | 98.16 | kPa | 429.54 | Vapor p... |
| Pvap | 101.30 | kPa | 430.11 | Vapor-l... |
| Pvap | 105.46 | kPa | 431.85 | Vapor p... |
| Pvap | 106.75 | kPa | 432.25 | Vapor p... |
| Pvap | 106.98 | kPa | 432.32 | Vapor p... |
| n0 | [1.41270; 1.42070] | [293.10; 313.15] |
|
|
|
T(K) Refractive Index 1.41 1.41 1.42 1.42 1.42 295 300 305 310 | ||||
| n0 | 1.41800 | 293.10 | Viscosi... | |
| n0 | 1.41830 | 293.15 | Densiti... | |
| n0 | 1.41800 | 293.15 | ERAS mo... | |
| n0 | 1.41826 | 293.15 | Excess ... | |
| n0 | 1.41807 | 293.15 | Densiti... | |
| n0 | 1.41750 | 293.15 | Measure... | |
| n0 | 1.41826 | 293.15 | Densiti... | |
| n0 | 1.41780 | 293.15 | Densiti... | |
| n0 | 1.41780 | 293.15 | Densiti... | |
| n0 | 1.41810 | 293.20 | Liquid-... | |
| n0 | 1.42070 | 293.20 | Vapor L... | |
| n0 | 1.41650 | 298.15 | Excess ... | |
| n0 | 1.41600 | 298.15 | Compara... | |
| n0 | 1.41610 | 298.15 | Densiti... | |
| n0 | 1.41580 | 298.15 | Liquid ... | |
| n0 | 1.41738 | 298.15 | Atmosph... | |
| n0 | 1.41550 | 298.15 | Ternary... | |
| n0 | 1.41600 | 298.15 | Liquid-... | |
| n0 | 1.41620 | 298.15 | Phase e... | |
| n0 | 1.41590 | 298.15 | Density... | |
| n0 | 1.41660 | 298.15 | Excess ... | |
| n0 | 1.41570 | 298.15 | Effect ... | |
| n0 | 1.41570 | 298.15 | Vapor-L... | |
| n0 | 1.41550 | 298.20 | Ternary... | |
| n0 | 1.41570 | 303.15 | Compara... | |
| n0 | 1.41423 | 303.15 | Densiti... | |
| n0 | 1.41423 | 303.15 | Densiti... | |
| n0 | 1.41340 | 303.15 | Measure... | |
| n0 | 1.41410 | 308.15 | Compara... | |
| n0 | 1.41270 | 313.15 | Compara... | |
| ρl | [765.64; 827.82] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 760 770 780 790 800 810 820 830 300 320 340 360 | ||||
| ρl | 826.03 | kg/m3 | 283.15 | Excess ... |
| ρl | 825.94 | kg/m3 | 283.15 | Densiti... |
| ρl | 827.82 | kg/m3 | 283.15 | Volumet... |
| ρl | 824.25 | kg/m3 | 288.15 | Volumet... |
| ρl | 822.42 | kg/m3 | 288.15 | Densiti... |
| ρl | 822.00 | kg/m3 | 288.15 | Effect ... |
| ρl | 822.26 | kg/m3 | 288.15 | Volumet... |
| ρl | 822.26 | kg/m3 | 288.15 | Volumet... |
| ρl | 819.00 | kg/m3 | 293.00 | KDB |
| ρl | 818.70 | kg/m3 | 293.15 | Investi... |
| ρl | 818.70 | kg/m3 | 293.15 | Volumet... |
| ρl | 818.90 | kg/m3 | 293.15 | Density... |
| ρl | 818.75 | kg/m3 | 293.15 | Volume ... |
| ρl | 818.00 | kg/m3 | 293.15 | Densiti... |
| ρl | 820.65 | kg/m3 | 293.15 | Volumet... |
| ρl | 819.00 | kg/m3 | 293.15 | Effect ... |
| ρl | 818.88 | kg/m3 | 293.15 | Densiti... |
| ρl | 818.70 | kg/m3 | 293.15 | Correla... |
| ρl | 818.69 | kg/m3 | 293.15 | Volumet... |
| ρl | 815.16 | kg/m3 | 298.10 | Excess ... |
| ρl | 815.34 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.02 | kg/m3 | 298.15 | Surface... |
| ρl | 815.30 | kg/m3 | 298.15 | Bubble ... |
| ρl | 815.21 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.10 | kg/m3 | 298.15 | Investi... |
| ρl | 815.10 | kg/m3 | 298.15 | Correla... |
| ρl | 814.94 | kg/m3 | 298.15 | Phase b... |
| ρl | 815.32 | kg/m3 | 298.15 | Densiti... |
| ρl | 815.50 | kg/m3 | 298.15 | Viscosi... |
| ρl | 815.26 | kg/m3 | 298.15 | Studies... |
| ρl | 814.94 | kg/m3 | 298.15 | Phase b... |
| ρl | 815.19 | kg/m3 | 298.15 | Volume ... |
| ρl | 815.30 | kg/m3 | 298.15 | Bubble ... |
| ρl | 815.40 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.70 | kg/m3 | 298.15 | Thermod... |
| ρl | 814.95 | kg/m3 | 298.15 | Densiti... |
| ρl | 815.65 | kg/m3 | 298.15 | Thermod... |
| ρl | 815.31 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 815.30 | kg/m3 | 298.15 | Density... |
| ρl | 815.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.29 | kg/m3 | 298.15 | Densiti... |
| ρl | 817.03 | kg/m3 | 298.15 | Volumet... |
| ρl | 815.15 | kg/m3 | 298.15 | Speeds ... |
| ρl | 815.00 | kg/m3 | 298.15 | Effect ... |
| ρl | 815.90 | kg/m3 | 298.15 | Excess ... |
| ρl | 815.11 | kg/m3 | 298.15 | Volumet... |
| ρl | 814.90 | kg/m3 | 298.15 | Densiti... |
| ρl | 815.20 | kg/m3 | 298.15 | Effect ... |
| ρl | 815.12 | kg/m3 | 298.15 | Volumet... |
| ρl | 815.88 | kg/m3 | 298.20 | Isother... |
| ρl | 815.17 | kg/m3 | 298.20 | Liquid-... |
| ρl | 811.60 | kg/m3 | 303.15 | Volume ... |
| ρl | 811.51 | kg/m3 | 303.15 | Volumet... |
| ρl | 811.52 | kg/m3 | 303.15 | Volumet... |
| ρl | 811.74 | kg/m3 | 303.15 | Densiti... |
| ρl | 811.50 | kg/m3 | 303.15 | Investi... |
| ρl | 813.39 | kg/m3 | 303.15 | Volumet... |
| ρl | 812.00 | kg/m3 | 303.15 | Effect ... |
| ρl | 811.50 | kg/m3 | 303.15 | Correla... |
| ρl | 811.39 | kg/m3 | 303.15 | Excess ... |
| ρl | 811.70 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 811.70 | kg/m3 | 303.15 | Density... |
| ρl | 811.30 | kg/m3 | 303.15 | Densiti... |
| ρl | 808.40 | kg/m3 | 308.15 | Viscosi... |
| ρl | 808.00 | kg/m3 | 308.15 | Effect ... |
| ρl | 809.71 | kg/m3 | 308.15 | Volumet... |
| ρl | 807.60 | kg/m3 | 308.15 | Densiti... |
| ρl | 808.06 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 807.98 | kg/m3 | 308.15 | Volume ... |
| ρl | 808.10 | kg/m3 | 308.15 | Density... |
| ρl | 807.89 | kg/m3 | 308.15 | Volumet... |
| ρl | 807.88 | kg/m3 | 308.15 | Volumet... |
| ρl | 807.90 | kg/m3 | 308.15 | Correla... |
| ρl | 808.13 | kg/m3 | 308.15 | Densiti... |
| ρl | 807.90 | kg/m3 | 308.15 | Investi... |
| ρl | 804.50 | kg/m3 | 313.15 | Densiti... |
| ρl | 806.00 | kg/m3 | 313.15 | Volumet... |
| ρl | 803.90 | kg/m3 | 313.15 | Densiti... |
| ρl | 804.20 | kg/m3 | 313.15 | Investi... |
| ρl | 804.50 | kg/m3 | 313.15 | Density... |
| ρl | 804.23 | kg/m3 | 313.15 | Volumet... |
| ρl | 804.46 | kg/m3 | 313.15 | Excess ... |
| ρl | 804.20 | kg/m3 | 313.15 | Correla... |
| ρl | 805.00 | kg/m3 | 313.15 | Effect ... |
| ρl | 804.25 | kg/m3 | 313.15 | Volumet... |
| ρl | 804.34 | kg/m3 | 313.15 | Volume ... |
| ρl | 800.60 | kg/m3 | 318.15 | Investi... |
| ρl | 802.27 | kg/m3 | 318.15 | Volumet... |
| ρl | 800.80 | kg/m3 | 318.15 | Density... |
| ρl | 800.56 | kg/m3 | 318.15 | Volumet... |
| ρl | 800.60 | kg/m3 | 318.15 | Correla... |
| ρl | 800.56 | kg/m3 | 318.15 | Volumet... |
| ρl | 801.00 | kg/m3 | 318.15 | Viscosi... |
| ρl | 800.66 | kg/m3 | 318.15 | Volume ... |
| ρl | 800.10 | kg/m3 | 318.15 | Densiti... |
| ρl | 800.60 | kg/m3 | 318.15 | Effect ... |
| ρl | 800.83 | kg/m3 | 318.15 | Densiti... |
| ρl | 796.20 | kg/m3 | 323.15 | Densiti... |
| ρl | 796.80 | kg/m3 | 323.15 | Investi... |
| ρl | 797.12 | kg/m3 | 323.15 | Densiti... |
| ρl | 796.85 | kg/m3 | 323.15 | Volumet... |
| ρl | 796.85 | kg/m3 | 323.15 | Volumet... |
| ρl | 796.80 | kg/m3 | 323.15 | Correla... |
| ρl | 797.10 | kg/m3 | 323.15 | Density... |
| ρl | 798.49 | kg/m3 | 323.15 | Volumet... |
| ρl | 798.00 | kg/m3 | 323.15 | Effect ... |
| ρl | 793.37 | kg/m3 | 328.15 | Densiti... |
| ρl | 793.20 | kg/m3 | 328.15 | Effect ... |
| ρl | 793.40 | kg/m3 | 328.15 | Density... |
| ρl | 794.67 | kg/m3 | 328.15 | Volumet... |
| ρl | 793.50 | kg/m3 | 328.15 | Viscosi... |
| ρl | 791.00 | kg/m3 | 333.15 | Effect ... |
| ρl | 789.57 | kg/m3 | 333.15 | Densiti... |
| ρl | 790.80 | kg/m3 | 333.15 | Volumet... |
| ρl | 785.50 | kg/m3 | 338.15 | Effect ... |
| ρl | 785.90 | kg/m3 | 338.15 | Viscosi... |
| ρl | 785.72 | kg/m3 | 338.15 | Densiti... |
| ρl | 783.00 | kg/m3 | 343.15 | Effect ... |
| ρl | 781.83 | kg/m3 | 343.15 | Densiti... |
| ρl | 777.86 | kg/m3 | 348.15 | Densiti... |
| ρl | 773.86 | kg/m3 | 353.15 | Densiti... |
| ρl | 769.78 | kg/m3 | 358.15 | Densiti... |
| ρl | 765.64 | kg/m3 | 363.15 | Densiti... |
| ΔfusS | 68.11 | J/mol×K | 225.80 | NIST |
| csound,fluid | [1237.50; 1339.20] | m/s | [288.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1240 1260 1280 1300 1320 1340 290 300 310 | ||||
| csound,fluid | 1339.20 | m/s | 288.15 | Ultraso... |
| csound,fluid | 1320.38 | m/s | 293.15 | Thermod... |
| csound,fluid | 1320.11 | m/s | 293.15 | Densiti... |
| csound,fluid | 1321.20 | m/s | 293.15 | Ultraso... |
| csound,fluid | 1312.40 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1306.90 | m/s | 298.15 | Ultraso... |
| csound,fluid | 1303.19 | m/s | 298.15 | Densiti... |
| csound,fluid | 1303.54 | m/s | 298.15 | Thermod... |
| csound,fluid | 1289.50 | m/s | 303.15 | Ultraso... |
| csound,fluid | 1286.68 | m/s | 303.15 | Thermod... |
| csound,fluid | 1275.70 | m/s | 308.15 | Ultraso... |
| csound,fluid | 1270.00 | m/s | 308.15 | Thermod... |
| csound,fluid | 1256.30 | m/s | 313.15 | Ultraso... |
| csound,fluid | 1253.54 | m/s | 313.15 | Thermod... |
| csound,fluid | 1237.50 | m/s | 318.15 | Ultraso... |
| γ | [0.02; 0.03] | N/m | [288.15; 328.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.03 0.03 290 300 310 320 | ||||
| γ | 0.03 | N/m | 288.15 | Density... |
| γ | 0.03 | N/m | 288.15 | Density... |
| γ | 0.03 | N/m | 288.15 | The add... |
| γ | 0.03 | N/m | 288.15 | Study o... |
| γ | 0.03 | N/m | 293.15 | Density... |
| γ | 0.03 | N/m | 293.15 | The add... |
| γ | 0.03 | N/m | 298.15 | Density... |
| γ | 0.02 | N/m | 298.15 | Study o... |
| γ | 0.03 | N/m | 298.15 | Density... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 298.15 | The add... |
| γ | 0.03 | N/m | 298.20 | KDB |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.03 | N/m | 303.15 | The add... |
| γ | 0.02 | N/m | 303.15 | Density... |
| γ | 0.02 | N/m | 308.15 | Study o... |
| γ | 0.02 | N/m | 308.15 | Density... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | The add... |
| γ | 0.02 | N/m | 308.15 | Density... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | The add... |
| γ | 0.02 | N/m | 318.15 | The add... |
| γ | 0.02 | N/m | 318.15 | Study o... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| γ | 0.02 | N/m | 328.15 | Study o... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 818.6 |
| 293.15 | 10000.00 | 824.8 |
| 293.15 | 20000.00 | 830.9 |
| 293.15 | 30000.00 | 836.4 |
| 293.15 | 40000.00 | 841.6 |
| 293.15 | 50000.00 | 846.5 |
| 293.15 | 60000.00 | 851.1 |
| 293.15 | 70000.00 | 855.5 |
| 293.15 | 80000.00 | 859.8 |
| 293.15 | 90000.00 | 863.7 |
| 293.15 | 100000.00 | 867.9 |
| 293.15 | 110000.00 | 871.5 |
| 293.15 | 120000.00 | 875.2 |
| 293.15 | 130000.00 | 878.7 |
| 293.15 | 140000.00 | 882.2 |
| 303.15 | 100.00 | 811.5 |
| 303.15 | 10000.00 | 818.2 |
| 303.15 | 20000.00 | 824.1 |
| 303.15 | 30000.00 | 830.0 |
| 303.15 | 40000.00 | 835.1 |
| 303.15 | 50000.00 | 840.5 |
| 303.15 | 60000.00 | 845.3 |
| 303.15 | 70000.00 | 849.8 |
| 303.15 | 80000.00 | 854.2 |
| 303.15 | 90000.00 | 858.4 |
| 303.15 | 100000.00 | 862.4 |
| 303.15 | 110000.00 | 866.3 |
| 303.15 | 120000.00 | 870.0 |
| 303.15 | 130000.00 | 873.6 |
| 303.15 | 140000.00 | 877.1 |
| 313.15 | 100.00 | 804.2 |
| 313.15 | 10000.00 | 811.1 |
| 313.15 | 20000.00 | 817.4 |
| 313.15 | 30000.00 | 823.5 |
| 313.15 | 40000.00 | 829.0 |
| 313.15 | 50000.00 | 834.4 |
| 313.15 | 60000.00 | 839.4 |
| 313.15 | 70000.00 | 844.3 |
| 313.15 | 80000.00 | 848.7 |
| 313.15 | 90000.00 | 853.1 |
| 313.15 | 100000.00 | 857.1 |
| 313.15 | 110000.00 | 861.2 |
| 313.15 | 120000.00 | 865.1 |
| 313.15 | 130000.00 | 868.7 |
| 313.15 | 140000.00 | 872.5 |
| 323.15 | 100.00 | 797.3 |
| 323.15 | 10000.00 | 804.5 |
| 323.15 | 20000.00 | 811.2 |
| 323.15 | 30000.00 | 817.4 |
| 323.15 | 40000.00 | 823.3 |
| 323.15 | 50000.00 | 828.7 |
| 323.15 | 60000.00 | 833.8 |
| 323.15 | 70000.00 | 838.5 |
| 323.15 | 80000.00 | 843.1 |
| 323.15 | 90000.00 | 847.6 |
| 323.15 | 100000.00 | 851.8 |
| 323.15 | 110000.00 | 856.0 |
| 323.15 | 120000.00 | 860.0 |
| 323.15 | 130000.00 | 863.7 |
| 323.15 | 140000.00 | 867.3 |
| 333.15 | 100.00 | 789.7 |
| 333.15 | 10000.00 | 797.2 |
| 333.15 | 20000.00 | 804.3 |
| 333.15 | 30000.00 | 810.8 |
| 333.15 | 40000.00 | 817.0 |
| 333.15 | 50000.00 | 822.7 |
| 333.15 | 60000.00 | 828.0 |
| 333.15 | 70000.00 | 832.8 |
| 333.15 | 80000.00 | 837.6 |
| 333.15 | 90000.00 | 842.5 |
| 333.15 | 100000.00 | 846.8 |
| 333.15 | 110000.00 | 850.8 |
| 333.15 | 120000.00 | 854.4 |
| 333.15 | 130000.00 | 858.5 |
| 333.15 | 140000.00 | 862.2 |
| 343.15 | 100.00 | 781.9 |
| 343.15 | 10000.00 | 790.2 |
| 343.15 | 20000.00 | 797.6 |
| 343.15 | 30000.00 | 804.4 |
| 343.15 | 40000.00 | 810.6 |
| 343.15 | 50000.00 | 816.4 |
| 343.15 | 60000.00 | 822.1 |
| 343.15 | 70000.00 | 827.3 |
| 343.15 | 80000.00 | 832.1 |
| 343.15 | 90000.00 | 836.9 |
| 343.15 | 100000.00 | 841.4 |
| 343.15 | 110000.00 | 845.7 |
| 343.15 | 120000.00 | 849.7 |
| 343.15 | 130000.00 | 853.6 |
| 343.15 | 140000.00 | 857.5 |
| 353.15 | 100.00 | 773.8 |
| 353.15 | 10000.00 | 782.3 |
| 353.15 | 20000.00 | 790.1 |
| 353.15 | 30000.00 | 797.3 |
| 353.15 | 40000.00 | 803.8 |
| 353.15 | 50000.00 | 810.0 |
| 353.15 | 60000.00 | 815.6 |
| 353.15 | 70000.00 | 821.0 |
| 353.15 | 80000.00 | 826.2 |
| 353.15 | 90000.00 | 831.1 |
| 353.15 | 100000.00 | 835.6 |
| 353.15 | 110000.00 | 840.0 |
| 353.15 | 120000.00 | 844.3 |
| 353.15 | 130000.00 | 848.4 |
| 353.15 | 140000.00 | 852.3 |
| 363.15 | 100.00 | 765.5 |
| 363.15 | 10000.00 | 774.9 |
| 363.15 | 20000.00 | 783.1 |
| 363.15 | 30000.00 | 790.6 |
| 363.15 | 40000.00 | 797.5 |
| 363.15 | 50000.00 | 803.8 |
| 363.15 | 60000.00 | 809.7 |
| 363.15 | 70000.00 | 815.4 |
| 363.15 | 80000.00 | 820.6 |
| 363.15 | 90000.00 | 825.6 |
| 363.15 | 100000.00 | 830.3 |
| 363.15 | 110000.00 | 834.8 |
| 363.15 | 120000.00 | 839.2 |
| 363.15 | 130000.00 | 843.3 |
| 363.15 | 140000.00 | 847.2 |
| 373.15 | 100.00 | 756.9 |
| 373.15 | 10000.00 | 766.6 |
| 373.15 | 20000.00 | 775.4 |
| 373.15 | 30000.00 | 783.4 |
| 373.15 | 40000.00 | 790.4 |
| 373.15 | 50000.00 | 796.9 |
| 373.15 | 60000.00 | 803.1 |
| 373.15 | 70000.00 | 808.9 |
| 373.15 | 80000.00 | 814.2 |
| 373.15 | 90000.00 | 819.5 |
| 373.15 | 100000.00 | 824.4 |
| 373.15 | 110000.00 | 829.2 |
| 373.15 | 120000.00 | 833.3 |
| 373.15 | 130000.00 | 837.7 |
| 373.15 | 140000.00 | 841.7 |
| 383.15 | 100.00 | 748.2 |
| 383.15 | 10000.00 | 759.1 |
| 383.15 | 20000.00 | 767.8 |
| 383.15 | 30000.00 | 776.5 |
| 383.15 | 40000.00 | 783.5 |
| 383.15 | 50000.00 | 790.4 |
| 383.15 | 60000.00 | 796.8 |
| 383.15 | 70000.00 | 802.6 |
| 383.15 | 80000.00 | 808.3 |
| 383.15 | 90000.00 | 813.7 |
| 383.15 | 100000.00 | 818.7 |
| 383.15 | 110000.00 | 823.4 |
| 383.15 | 120000.00 | 828.0 |
| 383.15 | 130000.00 | 832.3 |
| 383.15 | 140000.00 | 836.5 |
| 393.15 | 100.00 | 739.4 |
| 393.15 | 10000.00 | 750.8 |
| 393.15 | 20000.00 | 760.5 |
| 393.15 | 30000.00 | 768.8 |
| 393.15 | 40000.00 | 777.0 |
| 393.15 | 50000.00 | 783.7 |
| 393.15 | 60000.00 | 790.3 |
| 393.15 | 70000.00 | 796.5 |
| 393.15 | 80000.00 | 802.5 |
| 393.15 | 90000.00 | 807.8 |
| 393.15 | 100000.00 | 813.0 |
| 393.15 | 110000.00 | 818.1 |
| 393.15 | 120000.00 | 822.6 |
| 393.15 | 130000.00 | 827.2 |
| 393.15 | 140000.00 | 831.5 |
| 403.15 | 100.00 | 730.2 |
| 403.15 | 10000.00 | 741.8 |
| 403.15 | 20000.00 | 751.9 |
| 403.15 | 30000.00 | 761.1 |
| 403.15 | 40000.00 | 769.3 |
| 403.15 | 50000.00 | 776.9 |
| 403.15 | 60000.00 | 783.7 |
| 403.15 | 70000.00 | 790.1 |
| 403.15 | 80000.00 | 796.2 |
| 403.15 | 90000.00 | 801.8 |
| 403.15 | 100000.00 | 807.2 |
| 403.15 | 110000.00 | 812.3 |
| 403.15 | 120000.00 | 817.1 |
| 403.15 | 130000.00 | 821.8 |
| 403.15 | 140000.00 | 826.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 815.1 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 828.9 |
| 278.15 | 1000.00 | 829.5 |
| 278.15 | 5000.00 | 832.0 |
| 278.15 | 10000.00 | 835.0 |
| 278.15 | 15000.00 | 838.0 |
| 278.15 | 20000.00 | 840.8 |
| 278.15 | 25000.00 | 843.6 |
| 278.15 | 30000.00 | 846.3 |
| 278.15 | 35000.00 | 848.9 |
| 278.15 | 40000.00 | 851.4 |
| 278.15 | 45000.00 | 853.9 |
| 278.15 | 50000.00 | 856.3 |
| 278.15 | 55000.00 | 858.7 |
| 278.15 | 60000.00 | 860.9 |
| 288.15 | 100.00 | 822.1 |
| 288.15 | 1000.00 | 822.7 |
| 288.15 | 5000.00 | 825.3 |
| 288.15 | 10000.00 | 828.5 |
| 288.15 | 15000.00 | 831.6 |
| 288.15 | 20000.00 | 834.6 |
| 288.15 | 25000.00 | 837.4 |
| 288.15 | 30000.00 | 840.2 |
| 288.15 | 35000.00 | 842.9 |
| 288.15 | 40000.00 | 845.5 |
| 288.15 | 45000.00 | 848.0 |
| 288.15 | 50000.00 | 850.5 |
| 288.15 | 55000.00 | 853.0 |
| 288.15 | 60000.00 | 855.4 |
| 298.15 | 100.00 | 814.9 |
| 298.15 | 1000.00 | 815.6 |
| 298.15 | 5000.00 | 818.4 |
| 298.15 | 10000.00 | 821.7 |
| 298.15 | 15000.00 | 824.9 |
| 298.15 | 20000.00 | 828.0 |
| 298.15 | 25000.00 | 830.9 |
| 298.15 | 30000.00 | 833.8 |
| 298.15 | 35000.00 | 836.6 |
| 298.15 | 40000.00 | 839.4 |
| 298.15 | 45000.00 | 842.0 |
| 298.15 | 50000.00 | 844.6 |
| 298.15 | 55000.00 | 847.1 |
| 298.15 | 60000.00 | 849.6 |
| 308.15 | 100.00 | 807.8 |
| 308.15 | 1000.00 | 808.4 |
| 308.15 | 5000.00 | 811.4 |
| 308.15 | 10000.00 | 814.8 |
| 308.15 | 15000.00 | 818.2 |
| 308.15 | 20000.00 | 821.4 |
| 308.15 | 25000.00 | 824.5 |
| 308.15 | 30000.00 | 827.5 |
| 308.15 | 35000.00 | 830.3 |
| 308.15 | 40000.00 | 833.2 |
| 308.15 | 45000.00 | 835.9 |
| 308.15 | 50000.00 | 838.5 |
| 308.15 | 55000.00 | 841.1 |
| 308.15 | 60000.00 | 843.5 |
| 318.15 | 100.00 | 800.5 |
| 318.15 | 1000.00 | 801.2 |
| 318.15 | 5000.00 | 804.3 |
| 318.15 | 10000.00 | 807.9 |
| 318.15 | 15000.00 | 811.4 |
| 318.15 | 20000.00 | 814.7 |
| 318.15 | 25000.00 | 817.9 |
| 318.15 | 30000.00 | 821.0 |
| 318.15 | 35000.00 | 824.0 |
| 318.15 | 40000.00 | 826.9 |
| 318.15 | 45000.00 | 829.7 |
| 318.15 | 50000.00 | 832.4 |
| 318.15 | 55000.00 | 835.1 |
| 318.15 | 60000.00 | 837.7 |
| 328.15 | 100.00 | 793.0 |
| 328.15 | 1000.00 | 793.7 |
| 328.15 | 5000.00 | 797.0 |
| 328.15 | 10000.00 | 800.8 |
| 328.15 | 15000.00 | 804.4 |
| 328.15 | 20000.00 | 807.9 |
| 328.15 | 25000.00 | 811.2 |
| 328.15 | 30000.00 | 814.4 |
| 328.15 | 35000.00 | 817.6 |
| 328.15 | 40000.00 | 820.6 |
| 328.15 | 45000.00 | 823.5 |
| 328.15 | 50000.00 | 826.4 |
| 328.15 | 55000.00 | 829.1 |
| 328.15 | 60000.00 | 831.6 |
| 338.15 | 100.00 | 785.4 |
| 338.15 | 1000.00 | 786.2 |
| 338.15 | 5000.00 | 789.6 |
| 338.15 | 10000.00 | 793.6 |
| 338.15 | 15000.00 | 797.4 |
| 338.15 | 20000.00 | 801.0 |
| 338.15 | 25000.00 | 804.5 |
| 338.15 | 30000.00 | 807.9 |
| 338.15 | 35000.00 | 811.1 |
| 338.15 | 40000.00 | 814.2 |
| 338.15 | 45000.00 | 817.3 |
| 338.15 | 50000.00 | 820.2 |
| 338.15 | 55000.00 | 823.1 |
| 338.15 | 60000.00 | 825.7 |
| 348.15 | 100.00 | 777.6 |
| 348.15 | 1000.00 | 778.4 |
| 348.15 | 5000.00 | 782.0 |
| 348.15 | 10000.00 | 786.2 |
| 348.15 | 15000.00 | 790.2 |
| 348.15 | 20000.00 | 794.1 |
| 348.15 | 25000.00 | 797.6 |
| 348.15 | 30000.00 | 801.2 |
| 348.15 | 35000.00 | 804.6 |
| 348.15 | 40000.00 | 807.8 |
| 348.15 | 45000.00 | 811.0 |
| 348.15 | 50000.00 | 814.0 |
| 348.15 | 55000.00 | 817.0 |
| 348.15 | 60000.00 | 819.7 |
| 358.15 | 100.00 | 769.4 |
| 358.15 | 1000.00 | 770.0 |
| 358.15 | 5000.00 | 774.2 |
| 358.15 | 10000.00 | 778.6 |
| 358.15 | 15000.00 | 782.8 |
| 358.15 | 20000.00 | 786.9 |
| 358.15 | 25000.00 | 790.7 |
| 358.15 | 30000.00 | 794.3 |
| 358.15 | 35000.00 | 797.9 |
| 358.15 | 40000.00 | 801.3 |
| 358.15 | 45000.00 | 804.6 |
| 358.15 | 50000.00 | 807.7 |
| 358.15 | 55000.00 | 810.8 |
| 358.15 | 60000.00 | 813.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 828.9 |
| 278.15 | 1000.00 | 829.5 |
| 278.15 | 5000.00 | 832.0 |
| 278.15 | 10000.00 | 835.0 |
| 278.15 | 15000.00 | 838.0 |
| 278.15 | 20000.00 | 840.8 |
| 278.15 | 25000.00 | 843.6 |
| 278.15 | 30000.00 | 846.3 |
| 278.15 | 35000.00 | 848.9 |
| 278.15 | 40000.00 | 851.4 |
| 278.15 | 45000.00 | 853.9 |
| 278.15 | 50000.00 | 856.3 |
| 278.15 | 55000.00 | 858.7 |
| 278.15 | 60000.00 | 860.9 |
| 288.15 | 100.00 | 822.1 |
| 288.15 | 1000.00 | 822.7 |
| 288.15 | 5000.00 | 825.3 |
| 288.15 | 10000.00 | 828.5 |
| 288.15 | 15000.00 | 831.6 |
| 288.15 | 20000.00 | 834.6 |
| 288.15 | 25000.00 | 837.4 |
| 288.15 | 30000.00 | 840.2 |
| 288.15 | 35000.00 | 842.9 |
| 288.15 | 40000.00 | 845.5 |
| 288.15 | 45000.00 | 848.0 |
| 288.15 | 50000.00 | 850.5 |
| 288.15 | 55000.00 | 853.0 |
| 288.15 | 60000.00 | 855.4 |
| 298.15 | 100.00 | 814.9 |
| 298.15 | 1000.00 | 815.6 |
| 298.15 | 5000.00 | 818.4 |
| 298.15 | 10000.00 | 821.7 |
| 298.15 | 15000.00 | 824.9 |
| 298.15 | 20000.00 | 828.0 |
| 298.15 | 25000.00 | 830.9 |
| 298.15 | 30000.00 | 833.8 |
| 298.15 | 35000.00 | 836.6 |
| 298.15 | 40000.00 | 839.4 |
| 298.15 | 45000.00 | 842.0 |
| 298.15 | 50000.00 | 844.6 |
| 298.15 | 55000.00 | 847.1 |
| 298.15 | 60000.00 | 849.6 |
| 308.15 | 100.00 | 807.8 |
| 308.15 | 1000.00 | 808.4 |
| 308.15 | 5000.00 | 811.4 |
| 308.15 | 10000.00 | 814.8 |
| 308.15 | 15000.00 | 818.2 |
| 308.15 | 20000.00 | 821.4 |
| 308.15 | 25000.00 | 824.5 |
| 308.15 | 30000.00 | 827.5 |
| 308.15 | 35000.00 | 830.3 |
| 308.15 | 40000.00 | 833.2 |
| 308.15 | 45000.00 | 835.9 |
| 308.15 | 50000.00 | 838.5 |
| 308.15 | 55000.00 | 841.1 |
| 308.15 | 60000.00 | 843.5 |
| 318.15 | 100.00 | 800.5 |
| 318.15 | 1000.00 | 801.2 |
| 318.15 | 5000.00 | 804.3 |
| 318.15 | 10000.00 | 807.9 |
| 318.15 | 15000.00 | 811.4 |
| 318.15 | 20000.00 | 814.7 |
| 318.15 | 25000.00 | 817.9 |
| 318.15 | 30000.00 | 821.0 |
| 318.15 | 35000.00 | 824.0 |
| 318.15 | 40000.00 | 826.9 |
| 318.15 | 45000.00 | 829.7 |
| 318.15 | 50000.00 | 832.4 |
| 318.15 | 55000.00 | 835.1 |
| 318.15 | 60000.00 | 837.7 |
| 328.15 | 100.00 | 793.0 |
| 328.15 | 1000.00 | 793.7 |
| 328.15 | 5000.00 | 797.0 |
| 328.15 | 10000.00 | 800.8 |
| 328.15 | 15000.00 | 804.4 |
| 328.15 | 20000.00 | 807.9 |
| 328.15 | 25000.00 | 811.2 |
| 328.15 | 30000.00 | 814.4 |
| 328.15 | 35000.00 | 817.6 |
| 328.15 | 40000.00 | 820.6 |
| 328.15 | 45000.00 | 823.5 |
| 328.15 | 50000.00 | 826.4 |
| 328.15 | 55000.00 | 829.1 |
| 328.15 | 60000.00 | 831.6 |
| 338.15 | 100.00 | 785.4 |
| 338.15 | 1000.00 | 786.2 |
| 338.15 | 5000.00 | 789.6 |
| 338.15 | 10000.00 | 793.6 |
| 338.15 | 15000.00 | 797.4 |
| 338.15 | 20000.00 | 801.0 |
| 338.15 | 25000.00 | 804.5 |
| 338.15 | 30000.00 | 807.9 |
| 338.15 | 35000.00 | 811.1 |
| 338.15 | 40000.00 | 814.2 |
| 338.15 | 45000.00 | 817.3 |
| 338.15 | 50000.00 | 820.2 |
| 338.15 | 55000.00 | 823.1 |
| 338.15 | 60000.00 | 825.7 |
| 348.15 | 100.00 | 777.6 |
| 348.15 | 1000.00 | 778.4 |
| 348.15 | 5000.00 | 782.0 |
| 348.15 | 10000.00 | 786.2 |
| 348.15 | 15000.00 | 790.2 |
| 348.15 | 20000.00 | 794.1 |
| 348.15 | 25000.00 | 797.6 |
| 348.15 | 30000.00 | 801.2 |
| 348.15 | 35000.00 | 804.6 |
| 348.15 | 40000.00 | 807.8 |
| 348.15 | 45000.00 | 811.0 |
| 348.15 | 50000.00 | 814.0 |
| 348.15 | 55000.00 | 817.0 |
| 348.15 | 60000.00 | 819.7 |
| 358.15 | 100.00 | 769.4 |
| 358.15 | 1000.00 | 770.0 |
| 358.15 | 5000.00 | 774.2 |
| 358.15 | 10000.00 | 778.6 |
| 358.15 | 15000.00 | 782.8 |
| 358.15 | 20000.00 | 786.9 |
| 358.15 | 25000.00 | 790.7 |
| 358.15 | 30000.00 | 794.3 |
| 358.15 | 35000.00 | 797.9 |
| 358.15 | 40000.00 | 801.3 |
| 358.15 | 45000.00 | 804.6 |
| 358.15 | 50000.00 | 807.7 |
| 358.15 | 55000.00 | 810.8 |
| 358.15 | 60000.00 | 813.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 815.1 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.14 | 1034.00 | 804.9 |
| 313.14 | 2032.00 | 805.6 |
| 313.14 | 3046.00 | 806.3 |
| 313.14 | 4016.00 | 807.0 |
| 313.14 | 5013.00 | 807.7 |
| 313.14 | 6035.00 | 808.4 |
| 313.14 | 7010.00 | 809.1 |
| 313.14 | 8036.00 | 809.8 |
| 313.14 | 9015.00 | 810.5 |
| 313.14 | 10002.00 | 811.2 |
| 313.14 | 11020.00 | 811.8 |
| 313.14 | 12017.00 | 812.5 |
| 313.14 | 13002.00 | 813.2 |
| 313.14 | 14016.00 | 813.8 |
| 313.14 | 15016.00 | 814.5 |
| 313.14 | 16009.00 | 815.1 |
| 313.14 | 17010.00 | 815.8 |
| 313.14 | 18010.00 | 816.4 |
| 313.14 | 19012.00 | 817.1 |
| 313.14 | 20019.00 | 817.7 |
| 313.14 | 21006.00 | 818.3 |
| 313.14 | 22037.00 | 818.9 |
| 313.14 | 23037.00 | 819.6 |
| 313.14 | 24010.00 | 820.2 |
| 313.14 | 25023.00 | 820.8 |
| 323.12 | 1021.00 | 797.6 |
| 323.12 | 2009.00 | 798.4 |
| 323.12 | 3003.00 | 799.1 |
| 323.12 | 4014.00 | 799.8 |
| 323.12 | 5025.00 | 800.6 |
| 323.12 | 6021.00 | 801.3 |
| 323.12 | 7032.00 | 802.1 |
| 323.12 | 8016.00 | 802.8 |
| 323.12 | 9016.00 | 803.5 |
| 323.12 | 10019.00 | 804.2 |
| 323.12 | 11015.00 | 805.0 |
| 323.12 | 12012.00 | 805.7 |
| 323.12 | 13015.00 | 806.3 |
| 323.12 | 14006.00 | 807.0 |
| 323.12 | 15002.00 | 807.7 |
| 323.12 | 16013.00 | 808.4 |
| 323.12 | 17016.00 | 809.1 |
| 323.12 | 18018.00 | 809.7 |
| 323.12 | 19000.00 | 810.4 |
| 323.12 | 20003.00 | 811.0 |
| 323.12 | 21009.00 | 811.7 |
| 323.12 | 22000.00 | 812.3 |
| 323.12 | 23002.00 | 813.0 |
| 323.12 | 24021.00 | 813.6 |
| 323.12 | 25004.00 | 814.3 |
| 333.01 | 1023.00 | 790.2 |
| 333.01 | 2011.00 | 791.0 |
| 333.01 | 3042.00 | 791.8 |
| 333.01 | 4000.00 | 792.6 |
| 333.01 | 5014.00 | 793.3 |
| 333.01 | 6004.00 | 794.1 |
| 333.01 | 7021.00 | 794.9 |
| 333.01 | 8012.00 | 795.7 |
| 333.01 | 9002.00 | 796.4 |
| 333.01 | 10004.00 | 797.2 |
| 333.01 | 11026.00 | 797.9 |
| 333.01 | 12020.00 | 798.7 |
| 333.01 | 13018.00 | 799.4 |
| 333.01 | 14009.00 | 800.1 |
| 333.01 | 15019.00 | 800.8 |
| 333.01 | 16017.00 | 801.6 |
| 333.01 | 17006.00 | 802.3 |
| 333.01 | 18018.00 | 803.0 |
| 333.01 | 19013.00 | 803.7 |
| 333.01 | 20037.00 | 804.4 |
| 333.01 | 21029.00 | 805.0 |
| 333.01 | 22008.00 | 805.7 |
| 333.01 | 23026.00 | 806.4 |
| 333.01 | 24019.00 | 807.0 |
| 333.01 | 25025.00 | 807.7 |
| 342.96 | 1036.00 | 782.9 |
| 342.96 | 2011.00 | 783.7 |
| 342.96 | 3012.00 | 784.5 |
| 342.96 | 4015.00 | 785.4 |
| 342.96 | 5007.00 | 786.2 |
| 342.96 | 6013.00 | 787.0 |
| 342.96 | 7039.00 | 787.8 |
| 342.96 | 8023.00 | 788.6 |
| 342.96 | 9022.00 | 789.4 |
| 342.96 | 10035.00 | 790.2 |
| 342.96 | 11017.00 | 791.0 |
| 342.96 | 12016.00 | 791.7 |
| 342.96 | 13023.00 | 792.5 |
| 342.96 | 14003.00 | 793.2 |
| 342.96 | 15009.00 | 793.9 |
| 342.96 | 16014.00 | 794.7 |
| 342.96 | 17038.00 | 795.4 |
| 342.96 | 18023.00 | 796.1 |
| 342.96 | 19015.00 | 796.8 |
| 342.96 | 20015.00 | 797.5 |
| 342.96 | 21026.00 | 798.1 |
| 342.96 | 22003.00 | 798.8 |
| 342.96 | 23005.00 | 799.5 |
| 342.96 | 24003.00 | 800.1 |
| 342.96 | 25031.00 | 800.8 |
| 352.86 | 1020.00 | 775.0 |
| 352.86 | 2012.00 | 775.9 |
| 352.86 | 3028.00 | 776.9 |
| 352.86 | 4014.00 | 777.7 |
| 352.86 | 5010.00 | 778.6 |
| 352.86 | 6028.00 | 779.5 |
| 352.86 | 7039.00 | 780.4 |
| 352.86 | 8000.00 | 781.2 |
| 352.86 | 9030.00 | 782.1 |
| 352.86 | 10033.00 | 782.9 |
| 352.86 | 11014.00 | 783.7 |
| 352.86 | 12017.00 | 784.5 |
| 352.86 | 13014.00 | 785.3 |
| 352.86 | 14011.00 | 786.1 |
| 352.86 | 15010.00 | 786.9 |
| 352.86 | 16023.00 | 787.7 |
| 352.86 | 17018.00 | 788.5 |
| 352.86 | 18016.00 | 789.3 |
| 352.86 | 19014.00 | 790.0 |
| 352.86 | 20021.00 | 790.8 |
| 352.86 | 21017.00 | 791.5 |
| 352.86 | 22038.00 | 792.3 |
| 352.86 | 23016.00 | 793.0 |
| 352.86 | 24020.00 | 793.7 |
| 352.86 | 25048.00 | 794.5 |
| 362.80 | 1011.00 | 767.0 |
| 362.80 | 2009.00 | 768.0 |
| 362.80 | 3024.00 | 769.0 |
| 362.80 | 4006.00 | 769.9 |
| 362.80 | 5021.00 | 770.8 |
| 362.80 | 6035.00 | 771.8 |
| 362.80 | 7009.00 | 772.6 |
| 362.80 | 8023.00 | 773.6 |
| 362.80 | 9041.00 | 774.5 |
| 362.80 | 10000.00 | 775.3 |
| 362.80 | 11014.00 | 776.2 |
| 362.80 | 12026.00 | 777.1 |
| 362.80 | 13045.00 | 777.9 |
| 362.80 | 14030.00 | 778.8 |
| 362.80 | 15012.00 | 779.6 |
| 362.80 | 16031.00 | 780.4 |
| 362.80 | 17003.00 | 781.2 |
| 362.80 | 18020.00 | 782.0 |
| 362.80 | 19033.00 | 782.8 |
| 362.80 | 20004.00 | 783.6 |
| 362.80 | 21006.00 | 784.4 |
| 362.80 | 22032.00 | 785.2 |
| 362.80 | 22989.00 | 785.9 |
| 362.80 | 24055.00 | 786.7 |
| 362.80 | 25035.00 | 787.5 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 829.2 |
| 278.15 | 5000.00 | 832.2 |
| 278.15 | 10000.00 | 835.1 |
| 278.15 | 15000.00 | 837.8 |
| 278.15 | 20000.00 | 840.7 |
| 283.15 | 100.00 | 825.8 |
| 283.15 | 5000.00 | 828.7 |
| 283.15 | 10000.00 | 831.6 |
| 283.15 | 15000.00 | 834.5 |
| 283.15 | 20000.00 | 837.4 |
| 288.15 | 100.00 | 822.1 |
| 288.15 | 5000.00 | 825.2 |
| 288.15 | 10000.00 | 828.2 |
| 288.15 | 15000.00 | 831.3 |
| 288.15 | 20000.00 | 834.0 |
| 293.15 | 100.00 | 818.7 |
| 293.15 | 5000.00 | 821.9 |
| 293.15 | 10000.00 | 824.9 |
| 293.15 | 15000.00 | 827.9 |
| 293.15 | 20000.00 | 830.7 |
| 298.15 | 100.00 | 815.1 |
| 298.15 | 5000.00 | 818.3 |
| 298.15 | 10000.00 | 821.5 |
| 298.15 | 15000.00 | 824.6 |
| 298.15 | 20000.00 | 827.5 |
| 303.15 | 100.00 | 811.4 |
| 303.15 | 5000.00 | 814.8 |
| 303.15 | 10000.00 | 818.0 |
| 303.15 | 15000.00 | 821.1 |
| 303.15 | 20000.00 | 824.2 |
| 308.15 | 100.00 | 808.0 |
| 308.15 | 5000.00 | 811.3 |
| 308.15 | 10000.00 | 814.6 |
| 308.15 | 15000.00 | 817.8 |
| 308.15 | 20000.00 | 820.9 |
| 313.15 | 100.00 | 804.2 |
| 313.15 | 5000.00 | 807.6 |
| 313.15 | 10000.00 | 811.0 |
| 313.15 | 15000.00 | 814.3 |
| 313.15 | 20000.00 | 817.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 825.6 |
| 100.00 | 288.15 | 822.2 |
| 100.00 | 293.15 | 818.6 |
| 100.00 | 298.15 | 815.0 |
| 100.00 | 303.15 | 811.4 |
| 100.00 | 308.15 | 807.8 |
| 100.00 | 313.15 | 804.1 |
| 100.00 | 318.15 | 800.5 |
| 100.00 | 323.15 | 796.8 |
| 5000.00 | 283.15 | 828.7 |
| 5000.00 | 288.15 | 825.2 |
| 5000.00 | 293.15 | 821.7 |
| 5000.00 | 298.15 | 818.2 |
| 5000.00 | 303.15 | 814.7 |
| 5000.00 | 308.15 | 811.1 |
| 5000.00 | 313.15 | 807.6 |
| 5000.00 | 318.15 | 804.0 |
| 5000.00 | 323.15 | 800.4 |
| 10000.00 | 283.15 | 831.7 |
| 10000.00 | 288.15 | 828.2 |
| 10000.00 | 293.15 | 824.9 |
| 10000.00 | 298.15 | 821.4 |
| 10000.00 | 303.15 | 817.9 |
| 10000.00 | 308.15 | 814.5 |
| 10000.00 | 313.15 | 811.0 |
| 10000.00 | 318.15 | 807.5 |
| 10000.00 | 323.15 | 803.9 |
| 20000.00 | 283.15 | 837.3 |
| 20000.00 | 288.15 | 834.1 |
| 20000.00 | 293.15 | 830.8 |
| 20000.00 | 298.15 | 827.4 |
| 20000.00 | 303.15 | 824.1 |
| 20000.00 | 308.15 | 820.8 |
| 20000.00 | 313.15 | 817.4 |
| 20000.00 | 318.15 | 814.0 |
| 20000.00 | 323.15 | 810.7 |
| 30000.00 | 283.15 | 842.7 |
| 30000.00 | 288.15 | 839.5 |
| 30000.00 | 293.15 | 836.3 |
| 30000.00 | 298.15 | 833.1 |
| 30000.00 | 303.15 | 829.9 |
| 30000.00 | 308.15 | 826.7 |
| 30000.00 | 313.15 | 823.5 |
| 30000.00 | 318.15 | 820.1 |
| 30000.00 | 323.15 | 816.9 |
| 40000.00 | 283.15 | 847.8 |
| 40000.00 | 288.15 | 844.7 |
| 40000.00 | 293.15 | 841.6 |
| 40000.00 | 298.15 | 838.5 |
| 40000.00 | 303.15 | 835.4 |
| 40000.00 | 308.15 | 832.3 |
| 40000.00 | 313.15 | 829.1 |
| 40000.00 | 318.15 | 825.9 |
| 40000.00 | 323.15 | 822.8 |
| 50000.00 | 283.15 | 852.6 |
| 50000.00 | 288.15 | 849.6 |
| 50000.00 | 293.15 | 846.6 |
| 50000.00 | 298.15 | 843.5 |
| 50000.00 | 303.15 | 840.5 |
| 50000.00 | 308.15 | 837.5 |
| 50000.00 | 313.15 | 834.4 |
| 50000.00 | 318.15 | 831.4 |
| 50000.00 | 323.15 | 828.2 |
| 60000.00 | 283.15 | 857.2 |
| 60000.00 | 288.15 | 854.3 |
| 60000.00 | 293.15 | 851.4 |
| 60000.00 | 298.15 | 848.3 |
| 60000.00 | 303.15 | 845.4 |
| 60000.00 | 308.15 | 842.4 |
| 60000.00 | 313.15 | 839.4 |
| 60000.00 | 318.15 | 836.4 |
| 60000.00 | 323.15 | 833.4 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 101.00 | 292.91 | 1320.79 |
| 30390.00 | 292.92 | 1465.73 |
| 45590.00 | 292.92 | 1525.8 |
| 60790.00 | 292.91 | 1581.37 |
| 75990.00 | 292.92 | 1633.75 |
| 91180.00 | 292.91 | 1682.67 |
| 101320.00 | 292.91 | 1713.2 |
| 101.00 | 308.15 | 1269.05 |
| 15200.00 | 308.15 | 1349.81 |
| 30390.00 | 308.15 | 1419.69 |
| 45590.00 | 308.15 | 1482.88 |
| 60790.00 | 308.15 | 1540.4 |
| 75990.00 | 308.15 | 1594.13 |
| 91180.00 | 308.16 | 1643.48 |
| 101320.00 | 308.16 | 1675.87 |
| 101.00 | 298.18 | 1302.75 |
| 15200.00 | 298.19 | 1381.46 |
| 30390.00 | 298.19 | 1449.11 |
| 45590.00 | 298.19 | 1510.11 |
| 60790.00 | 298.19 | 1566.83 |
| 75990.00 | 298.19 | 1619.35 |
| 91180.00 | 298.19 | 1668.5 |
| 101320.00 | 298.19 | 1699.28 |
| 101.00 | 313.13 | 1252.38 |
| 15200.00 | 313.14 | 1334.05 |
| 30390.00 | 313.14 | 1404.76 |
| 45590.00 | 313.14 | 1469.3 |
| 60790.00 | 313.14 | 1527.64 |
| 75990.00 | 313.14 | 1581.73 |
| 91180.00 | 313.14 | 1632.08 |
| 101320.00 | 313.14 | 1664.3 |
| 101.00 | 318.22 | 1235.52 |
| 15200.00 | 318.22 | 1318.81 |
| 30390.00 | 318.21 | 1390.85 |
| 45590.00 | 318.21 | 1456.0 |
| 60790.00 | 318.21 | 1514.43 |
| 75990.00 | 318.21 | 1569.15 |
| 91180.00 | 318.21 | 1620.49 |
| 101320.00 | 318.21 | 1653.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [328.27; 454.77] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.49468e+01 | |||
| Coefficient B | -3.55660e+03 | |||
| Coefficient C | -8.56520e+01 | |||
| Temperature range, min. | 328.27 | |||
| Temperature range, max. | 454.77 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 328.27 | Calculated Property |
| Pvap | 2.98 | kPa | 342.33 | Calculated Property |
| Pvap | 6.11 | kPa | 356.38 | Calculated Property |
| Pvap | 11.68 | kPa | 370.44 | Calculated Property |
| Pvap | 21.02 | kPa | 384.49 | Calculated Property |
| Pvap | 35.88 | kPa | 398.55 | Calculated Property |
| Pvap | 58.48 | kPa | 412.60 | Calculated Property |
| Pvap | 91.57 | kPa | 426.66 | Calculated Property |
| Pvap | 138.38 | kPa | 440.71 | Calculated Property |
| Pvap | 202.64 | kPa | 454.77 | Calculated Property |
| Pvap | [5.21e-05; 3364.66] | kPa | [228.55; 611.35] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.08932e+02 | |||
| Coefficient B | -1.08747e+04 | |||
| Coefficient C | -1.31440e+01 | |||
| Coefficient D | 3.48998e-06 | |||
| Temperature range, min. | 228.55 | |||
| Temperature range, max. | 611.35 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 600 | ||||
| Pvap | 5.21e-05 | kPa | 228.55 | Calculated Property |
| Pvap | 0.01 | kPa | 271.08 | Calculated Property |
| Pvap | 0.39 | kPa | 313.62 | Calculated Property |
| Pvap | 5.03 | kPa | 356.15 | Calculated Property |
| Pvap | 33.18 | kPa | 398.68 | Calculated Property |
| Pvap | 137.52 | kPa | 441.22 | Calculated Property |
| Pvap | 410.94 | kPa | 483.75 | Calculated Property |
| Pvap | 970.21 | kPa | 526.28 | Calculated Property |
| Pvap | 1926.83 | kPa | 568.82 | Calculated Property |
| Pvap | 3364.66 | kPa | 611.35 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Hexanol.
Mixtures
- Isopropyl Alcohol + 1-Hexanol
- Dimethyl Sulfoxide + 1-Hexanol
- Ethane, 1,2-dichloro- + 1-Hexanol
- Ethane, 1,2-dibromo- + 1-Hexanol
- Tetrachloroethylene + 1-Hexanol
- 1-Propanol, 2-methyl- + 1-Hexanol
- Isobutyl acetate + 1-Hexanol
- Isobutyl acetate + 1-Propanol, 2-methyl- + 1-Hexanol
- 1-Hexanol + Nonane
- 2-Butanone + Benzene, 1,3-dichloro- + 1-Hexanol
- 1-Octene + 1-Hexanol
- 2-Octanone + 1-Hexanol
- 2-Propanol, 1-propoxy- + 1-Hexanol
- Pentanoic acid, 4-oxo- + 1-Hexanol + Water
- 1-Hexanol + Simvastatin
- Cholesterol + 1-Hexanol
- Cholesterol + 1-Hexanol + Cyclohexane
- Acetonitrile + 1-Hexanol
- 2-Propenenitrile + 1-Hexanol
- Formamide, N,N-dimethyl- + 1-Hexanol
Find more mixtures with 1-Hexanol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
- Measurements of the Properties of Binary Mixtures of Dimethylsulphoxide (DMSO) with 1-Alkanols (C4, C6, C7) at 303.15K
- 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
- Liquid phase behavior of imidazolium-based ionic liquids with alcohols: effect of hydrogen bonding and non-polar interactions
- 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
- Density and surface tension variation with temperature for n-nonane + 1-hexanol
- Excess molar volumes of ternary mixtures of 1,3-dichlorobenzene and methyl ethyl ketone with 1-alkanols at 303.15K
- Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
- 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
- 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
- Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
- Vapour liquid equilibria, azeotropic data, excess enthalpies, activity coefficients at infinite dilution and solid liquid equilibria for binary alcohol ketone systems
- Isobaric vapour liquid equilibria of binary 1-propoxy-2-propanol mixtures with water and alcohols at reduced pressure
- Phase equilibria of (water + levunilic acid + alcohol) ternary systems
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Solubility of pyrene in simple and mixed solvent systems
- Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
- (Solid + liquid) and (liquid + liquid) phase equilibria study and correlation of the binary systems {N-butyl-3-methylpyridinium tosylate + water, or + an alcohol, or + a hydrocarbon}
- Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
- Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
- Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
- Liquid density of oxygenated additives to bio-fuels: 1-Hexanol at pressures up to 140 MPa and from 293.15 K to 403.15 K
- Solubility of triclosan and iodopropynyl butylcarbamate in pure alkanols at several temperatures
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Liquid-liquid equilibrium data for systems containing of formic acid, water, and primary normal alcohols at T = 298.2 K
- Liquid-liquid equilibrium data for ternary systems of water + lactic acid + C4-C7 alcohols at 298.2 K and atmospheric pressure
- (p, VE, T) Measurements of mixtures (DBE + alcohol) at temperaturesfrom (293.15 to 353.15) K and at pressures up to 140 MPa
- Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
- Liquid-liquid phase equilibria of ionic liquid solutions in the critical region: 1-Methyl-3-octylimidazolium tetrafluoroborate with1-pentanol or 1-hexanol
- Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
- Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
- 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.
- Vapor pressures and thermophysical properties of selected hexenols and recommended vapor pressure for hexan-1-ol
- 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
- Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
- Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
- The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
- Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
- Phase equilibria for ternary liquid systems of (water + carboxylic acid or alcohol + 1-hexanol) at T = 293.15 K: modelling considerations
- Excess molar volumes and viscosities of (1,1,2,2-tetrabromoethane + 1-alkanols) at T = (293.15 and 303.15) K
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrachloroethane and 1-alkanols binary mixtures
- (Liquid + liquid) phase equilibria of 1-alkyl-3-methylimidazolium methylsulfate with alcohols, or ethers, or ketones
- Densities, excess molar volumes, and refractive indices of 1,1,2,2-tetrabromoethane and 1-alkanols binary mixtures
- 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
- 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
- Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
- Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Studies on thermodynamic properties of binary mixtures of hexan-1-ol with halogenated compounds at T = (308.15 and 313.15) K
- Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
- Volumetric, acoustic, and viscometric studies of molecular interactions in binary mixtures of diethylene glycol monomethyl ether with 1-alkanols at temperatures from (293.15 to 308.15) K
- High-pressure phase equilibria in the (carbon dioxide + 1-hexanol) system
- Ultrasonic speeds and isentropic compressibilities of {difurylmethane + (C1 C6) n-alkanol} binary mixtures at T = 298.15 K
- Cloud point measurements of 1-butyl-2,3-dimethylimidazolium tetrafluoroborate with alcohols
- Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
- Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
- Volumetric and viscometric properties of binary mixtures of {methyl tert-butyl ether (MTBE) + alcohol} at several temperatures and p = 0.1 MPa: Experimental results and application of the ERAS model
- Volumetric properties and enthalpies of solution of alcohols CkH2k+1OH (k = 1, 2, 6) in 1-methyl-3-alkylimidazolium bis(trifluoromethylsulfonyl)imide {[C1CnIm][NTf2] n = 2, 4, 6, 8, 10} ionic liquids
- Excess molar enthalpies of binary systems containing 2-octanone, hexanoic acid, or octanoic acid at T = 298.15 K
- PrhoT measurements and derived properties of liquid 1-alkanols
- Comparative study of physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-alkanols at different temperatures
- 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
- Ternary equilibrium data of mixtures consisting of 2-butanol, water, and heavy alcohols at T = 298.2 K
- Studies of thermophysical properties of binary liquid mixtures of amine and alcohols at various temperatures
- Viscosity and surface tension of binary systems of N,N-dimethylformamide with alkan-1-ols at different temperatures
- Solubility of salicylic acid in pure alcohols at different temperatures
- Density, speed of sound, heat capacity, and related properties of 1-hexanol and 2-ethyl-1-butanol as function of temperature and pressure
- 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
- 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
- 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
- On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
- Study of surface tension and surface properties of binary systems of DMSO with long chain alcohols at various temperatures
- Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
- 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
- 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
- Application of the NRTL method to correlate solubility of diosgenin
- Solubility of climbazole in various alcohols at different temperatures
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Volumetric and viscometric study with FT-IR analysis of binary systems with diethyl succinate and alcohols
- Solubility of commercial octacosanol in organic solvents and their correlation by thermodynamic models at different temperatures
- Physical properties of systems of interest to the edible oil industry: Viscosities and densities of model systems formed by (triacylglycerol + fatty acid + solvent)
- High pressure liquid densities and excess volumes of the (di-isopropyl ether + 1-hexanol) system
- Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
- Volumetric and transport properties of binary liquid mixtures with 1-ethyl-3-methylimidazolium ethyl sulfate as candidate solvents for regenerative flue gas desulfurization processes
- FT-IR studies and excess thermodynamic properties of binary liquid mixtures 2-(2-butoxyethoxy) ethanol with 1-hexanol, 1-octanol and 1-decanol at different temperatures
- 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)
- The additivity of surface and volumetric properties of alpha,omega-dihalogenoalkanes
- Excess volumes and partial molar volumes of binary liquid mixtures of furfural or 2-methylfuran with alcohols at 298.15 K
- Liquid-liquid equilibrium for (water + 5-hydroxymethylfurfural + 1-pentanol/1-hexanol/1-heptanol) systems at 298.15 K
- Solubility and mixing thermodynamic properties of levamisole hydrochloride in twelve pure solvents at various temperatures
- Excess molar enthalpies of methyl isobutyl ketone (MIBK) with alkan-1-ols (C1-C6) and their correlations at 298.15 K
- Thermophysical properties and thermodynamic phase behavior of ionic liquids
- 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
- Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
- Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
- Densities, Viscosities, and Refractive Indices of Dimethyl Carbonate + 1-Hexanol/1-Octanol Binary Mixtures at Different Temperatures
- Thermodynamics of 1,3-dimethylurea in eight alcohols
- Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
- 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
- Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
- Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
- Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Investigation of Molecular Interactions in Binary Mixtures of n-Butyl Acetate and (C6 - C10) 1-Alkanol: PC-SAFT Model
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- 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
- Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Solubility Determination and Modeling of EGCG Peracetate in 12 Pure Solvents at Temperatures from 278.15 to 318.15 K
- Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
- Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
- Liquid-Liquid Equilibria for Ternary Mixtures of Water + Ethanol with 1-Hexanol, Butyl Propionate, or Ethyl Caproate
- Excess Molar Enthalpies of Propyl Propanoate + 1-Hexanol + Benzene at the Temperatures of 25 :C and 35 :C
- Solubility of Benzimidazoles in Alcohols
- 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.
- Density, Surface Tension, and Refractive Index of Octane + 1-Alkanol Mixtures at T ) 298.15 K.
- Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K
- 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
- Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
- Liquid-Liquid Equilibria for the Ternary Systems of (Water + Tetrahydrofuran + Polar Solvent) at 298.15 K
- Liquid-Liquid Equilibrium of MTBE + Ethanol + Water and MTBE + 1-Hexanol + Water over the Temperature Range of 288.15 to 308.15 K
- Solubility and Density of 2,6-Dimethylnaphthalene in C1-C7 1-Alkanols
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Phase Equlibria for Hexyl Acetate Reactive Distillation
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- 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
- 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)
- Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
- Compressed Liquid Densities and Excess Molar Volumes of CO2 + Hexan-1-ol Mixtures from (313 to 363) K and Pressures up to 25 MPa
- Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
- Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Fluid-Phase Behavior of {1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide, [C6mim][NTf2], + C2-C8 n-Alcohol} Mixtures: Liquid-Liquid Equilibrium and Excess Volumes
- 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
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
- Volumetric and Viscometric Behavior of the Binary System: (Hexan-1-ol + p-Xylene)
- Thermodynamic Parameters of Anionic Surfactant-Additive Systems at the Cloud Point
- Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
- 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
- Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
- Solubilities of Phloretin in 12 Solvents at Different Temperatures
- Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
- Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
- Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
- Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
- Liquid Phase Behavior of 1-Butyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide with 1-Butanol or Hexan-1-ol: Measurements of Coexistence Curves, Density, and Interfacial Tension
- 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
- Liquid Liquid Phase Behavior of Solutions of 1,3-Dimethylimidazolium- and 1-Methyl-3-propylimidazolium Bis((trifluoromethyl)sulphonyl)amide (C1,3mimNTf2) in n-Alkyl Alcohols
- Determination and Correlation of Solubilities of Lauric Acid in Eight Alcohols
- Isobaric Vapor Liquid Equilibria of Binary Systems (Propyl Acetate + 2-Methylbutan-1-ol), (Propyl Acetate + Hexan-1-ol), and (Propyl Acetate + Heptan-1-ol) at 101.3 kPa
- Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
- Volumetric and Viscometric Study of Binary Systems of Ethyl Butyrate with Alcohols
- 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
- 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
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Liquid Liquid Equilibrium for Ternary Systems Containing Water, Oleic Acid, and Alcohols at 313.15 K. Effect of Alcohol Chain Length
- 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
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- 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
- Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
- Liquid Liquid Equilibria for the Quaternary Systems of Water + N-Methyl-2-pyrrolidone + 1-Hexanol + NaCl, + KCl, or + KAc
- 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
- Setup and Validation of a PGT Measuring Device. Volumetric Behavior of the Mixture 1,8-Cineole + Ethanol
- Surface Properties of Binary Mixtures of Ethylene Glycol with a Series of Aliphatic Alcohols (1-Pentanol, 1-Hexanol, and 1-Heptanol)
- Measurement and Correlation of the Solubilities of m-Phthalic Acid in Monobasic Alcohols
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Thermodynamic Properties of Micellization of Sodium Dodecylbenzene Sulfonate in the Aqueous-Rich Region of 1-Pentanol and 1-Hexanol
- Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
- Vapor-Liquid Equilibria of Binary Mixtures Formed by Hexan-1-ol with Chloroethanes and Chloroethenes at 95.6 kPa
- Thermodynamic Properties of the Binary Mixture of Hexan-1-ol with m-Xylene at T = (303.15, 313.15, and 323.15) K
- Studies on Transport and Thermodynamic Properties of Binary Mixtures of Hexan-1-ol with Halogenated Compounds at 293.15 K
- Volumetric and Viscometric Properties of Binary Liquid Mixtures of Ethylene Glycol Monomethyl Ether + 1-Hexanol, 1-Octanol, and 1-Decanol at Temperatures of T = (293.15, 298.15, 303.15, and 308.15) K
- Measurement and Correlation of Solubilities of Decanedioic Acid in C4-C6 Alcohol Solvents
- Studies of Monohydric Alcohols in Aqueous Sodium Dodecyl Sulfate Solutions at T = (298.15 and 308.15) K
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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