- InChI
- InChI=1S/C7H8O/c8-6-7-4-2-1-3-5-7/h1-5,8H,6H2
- InChI Key
- WVDDGKGOMKODPV-UHFFFAOYSA-N
- Formula
- C7H8O
- SMILES
- OCc1ccccc1
- Molecular Weight1
- 108.14
- CAS
- 100-51-6
- Other Names
-
- (Hydroxymethyl)benzene
- .alpha.-hydroxytoluene
- .alpha.-toluenol
- BENZAL ALCOHOL
- BENZENEMETHANOL
- Bentalol
- Benzenecarbinol
- Benzenmethanol
- Benzoyl alcohol
- Benzyl Alkohol
- Benzylic alcohol
- Hydroxytoluene
- Methanol benzene
- Methanol, phenyl-
- NCI-C06111
- NSC 8044
- PHENYLMETHANOL
- Phenylcarbinol
- Phenylmethyl alcohol
- «alpha»-Hydroxytoluene
- «alpha»-Toluenol
- «alpha»-Hydroxytoluene
- «alpha»-Toluenol
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- 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).
- 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).
- 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.
- 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°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| PAff | 778.30 | kJ/mol | NIST |
| Tig | 709.26 | K | KDB |
| BasG | 748.00 | kJ/mol | NIST |
| ΔcH°liquid | [-3743.00; -3723.00] | kJ/mol |
|
| ΔcH°liquid | -3743.00 ± 2.80 | kJ/mol | NIST |
| ΔcH°liquid | -3736.90 | kJ/mol | NIST |
| ΔcH°liquid | -3723.00 | kJ/mol | NIST |
| ΔcH°liquid | -3724.00 | kJ/mol | NIST |
| ΔcH°liquid | -3731.00 | kJ/mol | NIST |
| μ | 1.70 | debye | KDB |
| Tflash,cc | 377.59 | K | KDB |
| Tflash,oc | 373.71 | K | KDB |
| ΔfG° | -16.35 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-113.70; -94.08] | kJ/mol |
|
| ΔfH°gas | -94.08 | kJ/mol | KDB |
| ΔfH°gas | -94.60 ± 3.00 | kJ/mol | NIST |
| ΔfH°gas | -100.70 | kJ/mol | NIST |
| ΔfH°gas | -113.70 | kJ/mol | NIST |
| ΔfH°gas | -106.70 | kJ/mol | NIST |
| ΔfH°liquid | [-174.00; -154.90] | kJ/mol |
|
| ΔfH°liquid | -154.90 ± 3.00 | kJ/mol | NIST |
| ΔfH°liquid | -161.00 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -174.00 | kJ/mol | NIST |
| ΔfH°liquid | -167.00 | kJ/mol | NIST |
| ΔfusH° | 12.02 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [60.29; 69.50] | kJ/mol |
|
| ΔvapH° | 65.50 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 64.80 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | Outlier 69.50 | kJ/mol | NIST |
| ΔvapH° | 60.30 | kJ/mol | NIST |
| ΔvapH° | 62.50 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 62.10 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 63.00 ± 2.20 | kJ/mol | NIST |
| ΔvapH° | 60.29 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 60.30 ± 0.40 | kJ/mol | NIST |
| IE | [8.26; 9.53] | eV |
|
| IE | 8.26 ± 0.05 | eV | NIST |
| IE | 8.37 | eV | NIST |
| IE | 9.00 ± 0.10 | eV | NIST |
| IE | 9.14 ± 0.05 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.53 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.11 | eV | NIST |
| log10WS | [-0.40; -0.40] |
|
|
| log10WS | -0.40 | Aq. Sol... | |
| log10WS | -0.40 | Estimat... | |
| logPoct/wat | 1.179 | Crippen Calculated Property | |
| McVol | 91.600 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 4300.00 | kPa | KDB |
| Inp | [167.20; 1082.00] |
|
|
| Inp | 1027.54 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1006.80 | NIST | |
| Inp | 1005.30 | NIST | |
| Inp | 1012.30 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1023.60 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1005.70 | NIST | |
| Inp | 1005.70 | NIST | |
| Inp | 1034.40 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1020.30 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1034.50 | NIST | |
| Inp | 1035.60 | NIST | |
| Inp | 1035.70 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1009.10 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1039.08 | NIST | |
| Inp | 1039.31 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1004.80 | NIST | |
| Inp | 1026.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1027.20 | NIST | |
| Inp | 1027.20 | NIST | |
| Inp | 1003.90 | NIST | |
| Inp | 1007.40 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1041.30 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1006.50 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1021.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1001.00 | NIST | |
| Inp | 1019.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1006.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1013.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1010.00 | NIST | |
| Inp | 1036.90 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1015.00 | NIST | |
| Inp | 1018.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1004.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | Outlier 167.20 | NIST | |
| Inp | 1023.60 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | Outlier 167.20 | NIST | |
| Inp | 1026.00 | NIST | |
| I | [1821.00; 1919.00] |
|
|
| I | 1895.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1887.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1886.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | 1834.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1830.00 | NIST | |
| I | Outlier 1821.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1887.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1904.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1895.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1881.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1864.00 | NIST | |
| I | Outlier 1821.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1823.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1902.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1825.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1907.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1849.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1852.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1846.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1872.30 | NIST | |
| I | 1876.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1848.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1835.00 | NIST | |
| I | 1859.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1890.00 | NIST | |
| I | Outlier 1915.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1856.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1851.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1909.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1845.00 | NIST | |
| I | Outlier 1919.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1912.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1886.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1873.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1881.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1826.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1860.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1855.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1881.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1849.00 | NIST | |
| I | Outlier 1821.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1876.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1830.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1836.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1903.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1879.00 | NIST | |
| I | 1840.00 | NIST | |
| I | 1841.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1826.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1895.00 | NIST | |
| I | 1900.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1898.00 | NIST | |
| I | 1828.00 | NIST | |
| I | 1890.00 | NIST | |
| I | 1883.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1897.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1854.00 | NIST | |
| I | 1868.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1858.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1891.00 | NIST | |
| I | Outlier 1821.00 | NIST | |
| I | 1866.00 | NIST | |
| I | 1869.00 | NIST | |
| I | 1889.00 | NIST | |
| I | 1899.00 | NIST | |
| I | 1878.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1831.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1885.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1853.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1887.00 | NIST | |
| I | 1888.00 | NIST | |
| I | 1839.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1865.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1896.00 | NIST | |
| I | 1867.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1871.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1870.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1837.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1884.00 | NIST | |
| I | 1857.00 | NIST | |
| I | 1872.00 | NIST | |
| I | 1872.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | 1908.00 | NIST | |
| I | 1877.00 | NIST | |
| I | 1893.00 | NIST | |
| I | 1891.00 | NIST | |
| I | 1845.00 | NIST | |
| I | 1862.00 | NIST | |
| I | 1834.00 | NIST | |
| I | 1874.00 | NIST | |
| I | 1894.00 | NIST | |
| I | 1861.00 | NIST | |
| I | 1864.00 | NIST | |
| I | 1882.00 | NIST | |
| I | 1853.00 | NIST | |
| I | Outlier 1822.00 | NIST | |
| I | 1880.00 | NIST | |
| I | 1829.00 | NIST | |
| I | 1833.00 | NIST | |
| I | 1905.00 | NIST | |
| I | 1844.00 | NIST | |
| I | 1841.00 | NIST | |
| S°liquid | 216.70 | J/mol×K | NIST |
| Tboil | 478.46 | K | KDB |
| Tc | [713.00; 715.00] | K |
|
| Tc | 715.00 | K | KDB |
| Tc | 713.00 | K | Vapor-l... |
| Tfus | [257.90; 258.10] | K |
|
| Tfus | 257.90 | K | KDB |
| Tfus | 258.10 | K | Aq. Sol... |
| Tfus | 258.10 | K | (Solid ... |
| Vc | 0.339 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [182.35; 232.07] | J/mol×K | [478.42; 678.50] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 500 550 600 650 | ||||
| Cp,gas | 182.35 | J/mol×K | 478.42 | Joback Calculated Property |
| Cp,gas | 191.96 | J/mol×K | 511.77 | Joback Calculated Property |
| Cp,gas | 201.02 | J/mol×K | 545.11 | Joback Calculated Property |
| Cp,gas | 209.53 | J/mol×K | 578.46 | Joback Calculated Property |
| Cp,gas | 217.53 | J/mol×K | 611.81 | Joback Calculated Property |
| Cp,gas | 225.03 | J/mol×K | 645.15 | Joback Calculated Property |
| Cp,gas | 232.07 | J/mol×K | 678.50 | Joback Calculated Property |
| Cp,liquid | [215.90; 223.60] | J/mol×K | [298.00; 307.50] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 216 218 220 222 224 300 305 | ||||
| Cp,liquid | 220.50 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 217.86 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 215.94 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 215.90 | J/mol×K | 298.50 | NIST |
| Cp,liquid | 223.60 | J/mol×K | 307.50 | NIST |
| η | [0.0027470; 0.0055500] | Pa×s | [298.15; 323.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.50e-3 3.00e-3 3.50e-3 4.00e-3 4.50e-3 5.00e-3 5.50e-3 300 310 320 | ||||
| η | 0.0055500 | Pa×s | 298.15 | Densiti... |
| η | 0.0051600 | Pa×s | 298.15 | Densiti... |
| η | 0.0052110 | Pa×s | 298.15 | Excess ... |
| η | 0.0046700 | Pa×s | 303.15 | Densiti... |
| η | 0.0046890 | Pa×s | 303.15 | Densiti... |
| η | 0.0046750 | Pa×s | 303.15 | Densiti... |
| η | 0.0041250 | Pa×s | 308.15 | Excess ... |
| η | 0.0040100 | Pa×s | 308.15 | Densiti... |
| η | 0.0040040 | Pa×s | 308.15 | Densiti... |
| η | 0.0040580 | Pa×s | 308.15 | Densiti... |
| η | 0.0035200 | Pa×s | 313.15 | Densiti... |
| η | 0.0035220 | Pa×s | 313.15 | Densiti... |
| η | 0.0035310 | Pa×s | 313.15 | Densiti... |
| η | 0.0031030 | Pa×s | 318.15 | Densiti... |
| η | 0.0027470 | Pa×s | 323.15 | Densiti... |
| ΔfusH | [8.79; 8.97] | kJ/mol | [257.60; 257.60] |
|
| ΔfusH | 8.79 | kJ/mol | 257.60 | NIST |
| ΔfusH | 8.79 | kJ/mol | 257.60 | NIST |
| ΔfusH | 8.97 | kJ/mol | 257.60 | NIST |
| ΔvapH | [54.60; 66.20] | kJ/mol | [303.00; 479.00] |
|
| ΔvapH | 61.50 | kJ/mol | 303.00 | NIST |
| ΔvapH | 66.20 | kJ/mol | 318.00 | NIST |
| ΔvapH | 54.60 | kJ/mol | 479.00 | NIST |
| Pvap | [2.72e-03; 0.10] | kPa | [282.20; 323.60] |
|
|
T(K) Vapor pressure (kPa) 0 0.02 0.04 0.06 0.08 0.1 290 300 310 320 | ||||
| Pvap | 2.72e-03 | kPa | 282.20 | Thermod... |
| Pvap | 3.06e-03 | kPa | 282.90 | Thermoc... |
| Pvap | 3.68e-03 | kPa | 285.20 | Thermod... |
| Pvap | 4.07e-03 | kPa | 285.90 | Thermoc... |
| Pvap | 5.16e-03 | kPa | 288.20 | Thermod... |
| Pvap | 5.32e-03 | kPa | 288.90 | Thermoc... |
| Pvap | 6.88e-03 | kPa | 291.20 | Thermod... |
| Pvap | 7.38e-03 | kPa | 292.10 | Thermoc... |
| Pvap | 8.90e-03 | kPa | 294.10 | Thermod... |
| Pvap | 9.83e-03 | kPa | 295.30 | Thermoc... |
| Pvap | 0.01 | kPa | 297.20 | Thermod... |
| Pvap | 0.01 | kPa | 298.20 | Thermoc... |
| Pvap | 0.01 | kPa | 298.60 | Thermod... |
| Pvap | 0.02 | kPa | 300.20 | Thermod... |
| Pvap | 0.02 | kPa | 301.20 | Thermoc... |
| Pvap | 0.02 | kPa | 302.80 | Thermoc... |
| Pvap | 0.02 | kPa | 303.20 | Thermod... |
| Pvap | 0.02 | kPa | 303.60 | Thermod... |
| Pvap | 0.02 | kPa | 305.20 | Thermod... |
| Pvap | 0.03 | kPa | 305.80 | Thermoc... |
| Pvap | 0.03 | kPa | 308.10 | Thermod... |
| Pvap | 0.03 | kPa | 308.60 | Thermod... |
| Pvap | 0.03 | kPa | 308.80 | Thermoc... |
| Pvap | 0.04 | kPa | 311.20 | Thermod... |
| Pvap | 0.04 | kPa | 311.70 | Thermoc... |
| Pvap | 0.05 | kPa | 313.60 | Thermod... |
| Pvap | 0.05 | kPa | 314.10 | Thermod... |
| Pvap | 0.05 | kPa | 314.90 | Thermoc... |
| Pvap | 0.07 | kPa | 318.10 | Thermoc... |
| Pvap | 0.07 | kPa | 318.60 | Thermod... |
| Pvap | 0.08 | kPa | 321.10 | Thermoc... |
| Pvap | 0.10 | kPa | 323.60 | Thermod... |
| n0 | [1.53180; 1.53810] | [298.15; 308.15] |
|
|
|
T(K) Refractive Index 1.53 1.53 1.53 1.54 1.54 1.54 1.54 300 305 | ||||
| n0 | 1.53780 | 298.15 | Density... | |
| n0 | 1.53770 | 298.15 | Enthalp... | |
| n0 | 1.53810 | 298.15 | Excess ... | |
| n0 | 1.53540 | 303.15 | Density... | |
| n0 | 1.53180 | 308.15 | Density... | |
| n0 | 1.53500 | 308.15 | Enthalp... | |
| n0 | 1.53421 | 308.15 | Densiti... | |
| ρl | [1011.30; 1045.60] | kg/m3 | [293.15; 333.15] |
|
|
T(K) Liquid Density (kg/m3) 1010 1015 1020 1025 1030 1035 1040 1045 300 310 320 330 | ||||
| ρl | 1045.21 | kg/m3 | 293.15 | The stu... |
| ρl | 1045.60 | kg/m3 | 293.15 | Experim... |
| ρl | 1041.00 | kg/m3 | 298.00 | KDB |
| ρl | 1041.05 | kg/m3 | 298.15 | FT-IR s... |
| ρl | 1041.46 | kg/m3 | 298.15 | Excess ... |
| ρl | 1043.53 | kg/m3 | 298.15 | Thermod... |
| ρl | 1041.80 | kg/m3 | 298.15 | Experim... |
| ρl | 1041.22 | kg/m3 | 298.15 | Measure... |
| ρl | 1041.38 | kg/m3 | 298.15 | The stu... |
| ρl | 1041.44 | kg/m3 | 298.15 | Thermod... |
| ρl | 1044.85 | kg/m3 | 298.15 | Densiti... |
| ρl | 1041.64 | kg/m3 | 298.15 | Densiti... |
| ρl | 1041.56 | kg/m3 | 298.15 | Effect ... |
| ρl | 1041.46 | kg/m3 | 298.15 | Thermod... |
| ρl | 1037.60 | kg/m3 | 303.15 | Effect ... |
| ρl | 1037.50 | kg/m3 | 303.15 | The stu... |
| ρl | 1037.15 | kg/m3 | 303.15 | FT-IR s... |
| ρl | 1037.35 | kg/m3 | 303.15 | Measure... |
| ρl | 1037.67 | kg/m3 | 303.15 | Thermod... |
| ρl | 1037.18 | kg/m3 | 303.15 | Study o... |
| ρl | 1037.42 | kg/m3 | 303.15 | Densiti... |
| ρl | 1033.30 | kg/m3 | 308.15 | Effect ... |
| ρl | 1033.75 | kg/m3 | 308.15 | Thermod... |
| ρl | 1033.70 | kg/m3 | 308.15 | Thermod... |
| ρl | 1033.47 | kg/m3 | 308.15 | Measure... |
| ρl | 1033.32 | kg/m3 | 308.15 | FT-IR s... |
| ρl | 1033.84 | kg/m3 | 308.15 | Densiti... |
| ρl | 1033.63 | kg/m3 | 308.15 | The stu... |
| ρl | 1033.45 | kg/m3 | 308.15 | Study o... |
| ρl | 1033.64 | kg/m3 | 308.50 | Excess ... |
| ρl | 1029.71 | kg/m3 | 313.15 | The stu... |
| ρl | 1030.00 | kg/m3 | 313.15 | Experim... |
| ρl | 1029.12 | kg/m3 | 313.15 | Effect ... |
| ρl | 1029.58 | kg/m3 | 313.15 | Measure... |
| ρl | 1029.46 | kg/m3 | 313.15 | FT-IR s... |
| ρl | 1029.91 | kg/m3 | 313.15 | Thermod... |
| ρl | 1029.36 | kg/m3 | 313.15 | Study o... |
| ρl | 1030.43 | kg/m3 | 313.15 | Densiti... |
| ρl | 1025.57 | kg/m3 | 318.15 | Study o... |
| ρl | 1025.59 | kg/m3 | 318.15 | FT-IR s... |
| ρl | 1025.67 | kg/m3 | 318.15 | Measure... |
| ρl | 1021.78 | kg/m3 | 323.15 | Study o... |
| ρl | 1021.75 | kg/m3 | 323.15 | Measure... |
| ρl | 1011.30 | kg/m3 | 333.15 | Experim... |
| ΔfusS | 34.82 | J/mol×K | 257.60 | NIST |
| γ | [0.04; 0.04] | N/m | [293.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.04 0.04 0.04 0.04 0.04 0.04 0.04 0.04 300 310 320 | ||||
| γ | 0.04 | N/m | 293.15 | Surface... |
| γ | 0.04 | N/m | 293.15 | Densiti... |
| γ | 0.04 | N/m | 293.15 | Surface... |
| γ | 0.04 | N/m | 293.15 | Equilib... |
| γ | 0.04 | N/m | 298.15 | Equilib... |
| γ | 0.04 | N/m | 298.15 | Densiti... |
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 298.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.04 | N/m | 303.15 | Densiti... |
| γ | 0.04 | N/m | 303.15 | Equilib... |
| γ | 0.04 | N/m | 303.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Densiti... |
| γ | 0.04 | N/m | 308.15 | Surface... |
| γ | 0.04 | N/m | 308.15 | Equilib... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Densiti... |
| γ | 0.04 | N/m | 313.15 | Surface... |
| γ | 0.04 | N/m | 313.15 | Equilib... |
| γ | 0.04 | N/m | 318.15 | Equilib... |
| γ | 0.04 | N/m | 318.15 | Surface... |
| γ | 0.04 | N/m | 318.15 | Surface... |
| γ | 0.04 | N/m | 318.15 | Densiti... |
| γ | 0.04 | N/m | 323.15 | Surface... |
| γ | 0.04 | N/m | 323.15 | Densiti... |
| γ | 0.04 | N/m | 323.15 | Equilib... |
| γ | 0.04 | N/m | 323.15 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [366.00; 366.20] | K | [1.30; 1.30] |
|
| Tboilr | 366.20 | K | 1.30 | NIST |
| Tboilr | 366.00 | K | 1.30 | NIST |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 81.50 | 1042.1 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [366.84; 503.99] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.62136e+01 | |||
| Coefficient B | -4.73989e+03 | |||
| Coefficient C | -6.92220e+01 | |||
| Temperature range, min. | 366.84 | |||
| Temperature range, max. | 503.99 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
| Pvap | 1.33 | kPa | 366.84 | Calculated Property |
| Pvap | 2.90 | kPa | 382.08 | Calculated Property |
| Pvap | 5.85 | kPa | 397.32 | Calculated Property |
| Pvap | 11.11 | kPa | 412.56 | Calculated Property |
| Pvap | 19.98 | kPa | 427.80 | Calculated Property |
| Pvap | 34.25 | kPa | 443.03 | Calculated Property |
| Pvap | 56.28 | kPa | 458.27 | Calculated Property |
| Pvap | 89.09 | kPa | 473.51 | Calculated Property |
| Pvap | 136.39 | kPa | 488.75 | Calculated Property |
| Pvap | 202.66 | kPa | 503.99 | Calculated Property |
| Pvap | [0.02; 4013.42] | kPa | [303.00; 711.66] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.81942e+01 | |||
| Coefficient B | -1.07272e+04 | |||
| Coefficient C | -9.93247e+00 | |||
| Coefficient D | 8.07990e-07 | |||
| Temperature range, min. | 303.00 | |||
| Temperature range, max. | 711.66 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 400 600 | ||||
| Pvap | 0.02 | kPa | 303.00 | Calculated Property |
| Pvap | 0.53 | kPa | 348.41 | Calculated Property |
| Pvap | 5.61 | kPa | 393.81 | Calculated Property |
| Pvap | 32.71 | kPa | 439.22 | Calculated Property |
| Pvap | 125.55 | kPa | 484.63 | Calculated Property |
| Pvap | 356.61 | kPa | 530.03 | Calculated Property |
| Pvap | 810.62 | kPa | 575.44 | Calculated Property |
| Pvap | 1557.31 | kPa | 620.85 | Calculated Property |
| Pvap | 2629.12 | kPa | 666.25 | Calculated Property |
| Pvap | 4013.42 | kPa | 711.66 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzyl alcohol.
Mixtures
- Benzyl alcohol + Benzene, 1-chloro-2-methyl-
- Benzene, 1-chloro-3-methyl- + Benzyl alcohol
- Benzyl alcohol + Benzene, 1-chloro-4-methyl-
- Benzene, 1-methyl-2-nitro- + Benzyl alcohol
- Benzyl alcohol + Benzene, 1-methyl-3-nitro-
- Benzyl alcohol + Thymol
- Aniline + Benzyl alcohol
- Aniline, N-methyl- + Benzyl alcohol
- Benzyl alcohol + Benzenamine, N,N-dimethyl-
- Benzyl alcohol + o-Chloroaniline
- Benzyl alcohol + m-Chloroaniline
- Benzyl alcohol + Ethanol, 2-methoxy-
- Benzyl alcohol + Ethanol, 2-ethoxy-
- Ethanol, 2-butoxy- + Benzyl alcohol
- Benzyl alcohol + 1,4-Benzenedicarboxaldehyde
- Benzyl alcohol + 1-Octanol
- Benzyl alcohol + 1-Decanol
- Benzyl alcohol + Acetic acid ethenyl ester
- Benzyl alcohol + Ethyl Acetate
- Benzyl alcohol + Acetic acid, 1,1-dimethylethyl ester
Find more mixtures with Benzyl alcohol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Thermodynamics of binary mixtures: The effect of substituents in aromatics on their excess properties with benzylalcohol
- Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method
- (Solid + liquid) equilibrium phase diagrams in binary mixtures containing terpenes: New experimental data and analysis of several modelling strategies with modified UNIFAC (Dortmund) and PC-SAFT equation of state
- Liquid-liquid equilibria for the extraction of furfural from aqueous solution using different solvents
- Study on thermo physical properties of binary mixture containing aromatic alcohol with aromatic, substituted aromatic amines at different temperatures interms of FT-IR, 1H NMR spectroscopic and DFT method
- Partial molar volumes of organic solutes in water. XI. Phenylmethanol and 2-phenylethanol at T=(298 to 573) K and at pressures up to 30 MPa
- Densities and excess volumes of binary mixtures of the ionic liquid 1-butyl-3-methylimidazolium hexafluorophosphate with aromatic compound at T = (298.15 to 313.15) K
- Densities and volumetric properties of binary mixtures of amino acid ionic liquid [bmim][Glu] or [bmim][Gly] with benzylalcohol at T = (298.15 to 313.15) K
- Solubilities of benzoic acid in binary (benzyl alcohol + benzaldehyde) solvent mixtures
- FT-IR spectroscopic study of excess thermodynamic properties of liquid mixtures containing benzylalcohol with alkoxyalkanols
- Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
- Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
- The study of excess molar volumes and related properties for binary mixtures containing benzyl alcohol and 1,3-dichloro-2-propanol with vinyl acetate, ethyl acetate and t-butyl acetate at T = 293.15 to 313.15 K and P = 0.087 MPa
- Experimental and Computational Thermodynamic Properties of (Benzyl alcohol + Alkanols) Mixtures
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- Effect of Diluents on Extraction Equilibrium of trans-Aconitic Acid
- Experimental High-Temperature, High-Pressure Density Measurement and Perturbed-Chain Statistical Associating Fluid Theory Modeling of Dimethyl Sulfoxide, Isoamyl Acetate, and Benzyl Alcohol
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Ethyl Chloroacetate + Cyclohexanone, + Chlorobenzene, + Bromobenzene, or + Benzyl Alcohol at (298.15, 303.15, and 308.15) K
- Densities and Viscosities of Binary Mixtures of N,N-Dimethylformamide with Benzyl Alcohol and Acetophenone at (298.15, 303.15, 308.15, and 313.15) K
- Thermodynamic Study of Binary Mixtures Containing Glycols or Polyethylene Glycols + Benzyl Alcohol at 308.15 K
- Equilibrium Surface Tensions of Benzyl Alcohol + Ethylene Glycol Mixtures
- Excess Properties of Binary Mixtures of Esters of Carbonic Acid + Three Aryl Alcohols at 308.15 K
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. Activity Coefficients of Ethers and Alcohols in 1-Methyl-3-Ethyl-Imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using the Transpiration Method
- Thermochemistry of Benzyl Alcohol: Reaction Equilibria Involving Benzyl Alcohol and tert-Alkyl Ethers
- Surface Tension of Dilute Solutions of Linear Alcohols in Benzyl Alcohol
- Enthalpies of Mixing, Densities, and Refractive Indices for Binary Mixtures of (Anisole or Phenetole) + Three Aryl Alcohols at 308.15 K and at Atmospheric Pressure
- Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
- Excess Enthalpies, Heat Capacities, Densities, Viscosities and Refractive Indices of Dimethyl Sulfoxide + Three Aryl Alcohols at 308.15 K and Atmospheric Pressure
- Excess Molar Enthalpies and Hydrogen Bonding in Binary Mixtures Containing Ethers and Benzyl Alcohol at 308.15 K and Atmospheric Pressure
- Excess Molar Enthalpies of Benzyl Alcohol + Alkanols (C1-C6) and Their Correlations at 298.15 K and Ambient Pressure
- Densities, Viscosities, and Refractive Properties of the Binary Mixtures of the Amino Acid Ionic Liquid [bmim][Ala] with Methanol or Benzylalcohol at T = (298.15 to 313.15) K
- Densities and Viscosities of the Binary Mixtures of Phenylmethanol with 2-Butanone
- Densities, Viscosities, Refractive Indexes, and Surface Tensions for Mixtures of Ethanol, Benzyl Acetate, and Benzyl Alcohol
- Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
- Solubility of CO2 in Nonaqueous Absorption System of 2-(2-Aminoethylamine)ethanol + Benzyl Alcohol
- Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Methylbenzene at (303.2 to 343.2) K
- Liquid Liquid Equilibria for the Ternary System Water + Benzyl Alcohol + Benzaldehyde at (303.2 to 343.2) K
- Solubilities of Benzoic Acid in Binary Methylbenzene + Benzyl Alcohol and Methylbenzene + Benzaldehyde Solvent Mixtures
- Measurement and Modeling of Volumetric Properties and Speeds of Sound of Several Mixtures of Alcohol Liquids Containing Butanediol
- Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary Mixtures of 2-Propanol + Benzyl Alcohol, + 2-Phenylethanol and Benzyl Alcohol + 2-Phenylethanol at T ) (298.15, 308.15, and 318.15) K
- Densities, Viscosities, Refractive Indices, and Surface Tensions for the Ternary Mixtures of 2-Propanol + Benzyl Alcohol + 2-Phenylethanol at T = 308.15 K
- Partitioning of Phenylalkanols between Micelles and Water Studied by Limiting Interdiffusion Coefficients in Water and Tetradecyltrimethylammonium Bromide Solutions
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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