- 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
- Bentalol
- Benzenmethanol
- Benzoyl alcohol
- Benzyl Alkohol
- Benzylic alcohol
- Hydroxytoluene
- Methanol benzene
- Methanol, phenyl-
- NCI-C06111
- NSC 8044
- benzenecarbinol
- benzenemethanol
- phenylcarbinol
- phenylmethanol
- phenylmethyl alcohol
- «alpha»-Hydroxytoluene
- «alpha»-Toluenol
- ω : Acentric Factor.
- 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).
- Ptriple : Triple Point 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).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3631 | ChemSep v8.3 pure component data | |
| 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; 1.71] | debye |
|
| μ | 1.71 | debye | ChemSep v8.3 pure component data |
| μ | 1.70 | debye | KDB |
| Tflash,cc | 377.59 | K | KDB |
| Tflash,oc | 373.71 | K | KDB |
| ΔfG° | -2.54 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | [-113.70; -90.25] | kJ/mol |
|
| ΔfH°gas | -90.25 | kJ/mol | ChemSep v8.3 pure component data |
| 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. Solubility Prediction | |
| log10WS | -0.40 | Estimated Solubility | |
| 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; 4374.00] | kPa |
|
| Pc | 4374.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 4300.00 | kPa | KDB |
| Ptriple | 1.88e-04 | kPa | ChemSep v8.3 pure component data |
| 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 | 1041.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1002.00 | NIST | |
| Inp | 1039.08 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1007.00 | NIST | |
| Inp | 1027.20 | NIST | |
| Inp | 1005.00 | NIST | |
| Inp | 1014.00 | NIST | |
| Inp | 1027.54 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1023.60 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | 1009.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1008.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | Outlier 167.20 | NIST | |
| Inp | 1012.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1022.00 | NIST | |
| Inp | 1003.00 | NIST | |
| Inp | 1081.00 | 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 | |
| I | 1895.00 | NIST | |
| I | 1875.00 | NIST | |
| I | 1887.00 | NIST | |
| S°liquid | 216.70 | J/mol×K | NIST |
| Tboil | [472.70; 478.95] | K |
|
| Tboil | 478.60 | K | ChemSep v8.3 pure component data |
| Tboil | 478.46 | K | KDB |
| Tboil | 477.20 | K | NIST |
| Tboil | 478.50 | K | NIST |
| Tboil | 478.40 | K | NIST |
| Tboil | 478.40 ± 0.50 | K | NIST |
| Tboil | 478.45 ± 0.40 | K | NIST |
| Tboil | 478.60 ± 0.25 | K | NIST |
| Tboil | 478.35 ± 0.40 | K | NIST |
| Tboil | 478.40 ± 0.50 | K | NIST |
| Tboil | 478.30 ± 0.50 | K | NIST |
| Tboil | 478.95 ± 0.50 | K | NIST |
| Tboil | 478.80 ± 0.30 | K | NIST |
| Tboil | 478.93 ± 0.15 | K | NIST |
| Tboil | Outlier 473.90 ± 1.50 | K | NIST |
| Tboil | Outlier 472.70 ± 1.50 | K | NIST |
| Tboil | 477.70 ± 1.00 | K | NIST |
| Tboil | 478.45 ± 1.00 | K | NIST |
| Tboil | 477.20 ± 3.00 | K | NIST |
| Tboil | 477.20 ± 3.00 | K | NIST |
| Tc | [713.00; 720.15] | K |
|
| Tc | 713.00 | K | Vapor-liquid critical point measurements of fifteen compounds by the pulse-heating method |
| Tc | 720.15 | K | ChemSep v8.3 pure component data |
| Tc | 715.00 | K | KDB |
| Tfus | [254.95; 258.10] | K |
|
| Tfus | 258.10 | K | (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 |
| Tfus | 257.85 | K | ChemSep v8.3 pure component data |
| Tfus | 257.90 | K | KDB |
| Tfus | 258.10 | K | Aq. Solubility Prediction |
| Tfus | 257.70 ± 0.60 | K | NIST |
| Tfus | 257.75 ± 0.30 | K | NIST |
| Tfus | 257.85 ± 0.20 | K | NIST |
| Tfus | 257.70 ± 0.30 | K | NIST |
| Tfus | 257.65 ± 0.30 | K | NIST |
| Tfus | 257.85 ± 0.40 | K | NIST |
| Tfus | 257.15 ± 0.40 | K | NIST |
| Tfus | Outlier 254.95 ± 0.60 | K | NIST |
| Tfus | 257.90 ± 0.40 | K | NIST |
| Ttriple | 257.85 | K | ChemSep v8.3 pure component data |
| UQi | 3.86 | ChemSep v8.3 pure component data | |
| URi | 4.70 | ChemSep v8.3 pure component data | |
| Vc | 0.382 | m3/kmol | ChemSep v8.3 pure component data |
| Zc | 0.2790000 | ChemSep v8.3 pure component data |
Temperature Dependent Properties
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 |
|---|---|---|---|---|
| Cp,gas | [96.34; 326.84] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.00000e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 5.99224e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 96.34 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 152.29 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 196.30 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 229.80 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 255.66 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 276.06 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 292.50 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 306.01 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 317.29 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 326.84 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [189.05; 276.17] | J/mol×K | [257.85; 478.60] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | -3.35000e+02 | |||
| Coefficient B | 3.64420e+00 | |||
| Coefficient C | -7.77510e-03 | |||
| Coefficient D | 5.91100e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidHeatCapacityCp | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 478.60 | |||
| Cp,liquid | 189.05 | J/mol×K | 257.85 | Calculated Property |
| Cp,liquid | 207.17 | J/mol×K | 282.38 | Calculated Property |
| Cp,liquid | 221.95 | J/mol×K | 306.91 | Calculated Property |
| Cp,liquid | 233.93 | J/mol×K | 331.43 | Calculated Property |
| Cp,liquid | 243.63 | J/mol×K | 355.96 | Calculated Property |
| Cp,liquid | 251.56 | J/mol×K | 380.49 | Calculated Property |
| Cp,liquid | 258.26 | J/mol×K | 405.02 | Calculated Property |
| Cp,liquid | 264.25 | J/mol×K | 429.54 | Calculated Property |
| Cp,liquid | 270.04 | J/mol×K | 454.07 | Calculated Property |
| Cp,liquid | 276.17 | J/mol×K | 478.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0209221; 0.0001821] | Pa×s | [257.85; 478.60] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.41520e+01 | |||
| Coefficient B | 2.65200e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 478.60 | |||
| η | 0.0209221 | Pa×s | 257.85 | Calculated Property |
| η | 0.0085628 | Pa×s | 282.38 | Calculated Property |
| η | 0.0040424 | Pa×s | 306.91 | Calculated Property |
| η | 0.0021326 | Pa×s | 331.43 | Calculated Property |
| η | 0.0012288 | Pa×s | 355.96 | Calculated Property |
| η | 0.0007601 | Pa×s | 380.49 | Calculated Property |
| η | 0.0004984 | Pa×s | 405.02 | Calculated Property |
| η | 0.0003429 | Pa×s | 429.54 | Calculated Property |
| η | 0.0002457 | Pa×s | 454.07 | Calculated Property |
| η | 0.0001821 | Pa×s | 478.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [68.80; 0.00] | kJ/mol | [257.85; 720.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 8.47620e+01 | |||
| Coefficient B | 3.52510e-01 | |||
| Coefficient C | 4.38530e-01 | |||
| Coefficient D | -3.02600e-01 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.20150e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 720.15 | |||
| ΔvapH | 68.80 | kJ/mol | 257.85 | Calculated Property |
| ΔvapH | 64.57 | kJ/mol | 309.22 | Calculated Property |
| ΔvapH | 60.05 | kJ/mol | 360.58 | Calculated Property |
| ΔvapH | 55.25 | kJ/mol | 411.95 | Calculated Property |
| ΔvapH | 50.13 | kJ/mol | 463.32 | Calculated Property |
| ΔvapH | 44.63 | kJ/mol | 514.68 | Calculated Property |
| ΔvapH | 38.59 | kJ/mol | 566.05 | Calculated Property |
| ΔvapH | 31.64 | kJ/mol | 617.42 | Calculated Property |
| ΔvapH | 22.71 | kJ/mol | 668.78 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 720.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [366.84; 503.99] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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 | |||
| 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 | [1.88e-04; 4371.55] | kPa | [257.85; 720.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 9.37722e+01 | |||
| Coefficient B | -1.10590e+04 | |||
| Coefficient C | -1.07090e+01 | |||
| Coefficient D | 3.05820e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 720.15 | |||
| Pvap | 1.88e-04 | kPa | 257.85 | Calculated Property |
| Pvap | 0.03 | kPa | 309.22 | Calculated Property |
| Pvap | 1.06 | kPa | 360.58 | Calculated Property |
| Pvap | 11.75 | kPa | 411.95 | Calculated Property |
| Pvap | 66.49 | kPa | 463.32 | Calculated Property |
| Pvap | 239.82 | kPa | 514.68 | Calculated Property |
| Pvap | 635.72 | kPa | 566.05 | Calculated Property |
| Pvap | 1364.81 | kPa | 617.42 | Calculated Property |
| Pvap | 2547.62 | kPa | 668.78 | Calculated Property |
| Pvap | 4371.55 | kPa | 720.15 | Calculated Property |
| Pvap | [0.02; 4013.42] | kPa | [303.00; 711.66] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.81942e+01 | |||
| Coefficient B | -1.07272e+04 | |||
| Coefficient C | -9.93247e+00 | |||
| Coefficient D | 8.07990e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 303.00 | |||
| Temperature range, max. | 711.66 | |||
| 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 |
| Pvap | [6.26; 101.62] | kPa | [395.67; 478.56] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.49141e+01 | |||
| Coefficient B | -4.00397e+03 | |||
| Coefficient C | -8.95590e+01 | |||
| Reference | Dreisbach and Shrader, 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 395.67 | |||
| Temperature range, max. | 478.56 | |||
| Pvap | 6.26 | kPa | 395.67 | Calculated Property |
| Pvap | 9.17 | kPa | 404.88 | Calculated Property |
| Pvap | 13.15 | kPa | 414.09 | Calculated Property |
| Pvap | 18.48 | kPa | 423.30 | Calculated Property |
| Pvap | 25.51 | kPa | 432.51 | Calculated Property |
| Pvap | 34.62 | kPa | 441.72 | Calculated Property |
| Pvap | 46.26 | kPa | 450.93 | Calculated Property |
| Pvap | 60.92 | kPa | 460.14 | Calculated Property |
| Pvap | 79.17 | kPa | 469.35 | Calculated Property |
| Pvap | 101.62 | kPa | 478.56 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1071.12; 283.33] | kg/m3 | [257.85; 720.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.47390e+01 | |||
| Coefficient B | 2.28490e-01 | |||
| Coefficient C | 7.20150e+02 | |||
| Coefficient D | 2.35670e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 720.15 | |||
| ρl | 1071.12 | kg/m3 | 257.85 | Calculated Property |
| ρl | 1032.83 | kg/m3 | 309.22 | Calculated Property |
| ρl | 992.26 | kg/m3 | 360.58 | Calculated Property |
| ρl | 948.87 | kg/m3 | 411.95 | Calculated Property |
| ρl | 901.84 | kg/m3 | 463.32 | Calculated Property |
| ρl | 849.90 | kg/m3 | 514.68 | Calculated Property |
| ρl | 790.86 | kg/m3 | 566.05 | Calculated Property |
| ρl | 720.23 | kg/m3 | 617.42 | Calculated Property |
| ρl | 625.76 | kg/m3 | 668.78 | Calculated Property |
| ρl | 283.33 | kg/m3 | 720.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [257.85; 720.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 6.87300e-02 | |||
| Coefficient B | 1.07900e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.20150e+02 | |||
| Comment | ChemSep eq 106, SurfaceTension | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 720.15 | |||
| γ | 0.04 | N/m | 257.85 | Calculated Property |
| γ | 0.04 | N/m | 309.22 | Calculated Property |
| γ | 0.03 | N/m | 360.58 | Calculated Property |
| γ | 0.03 | N/m | 411.95 | Calculated Property |
| γ | 0.02 | N/m | 463.32 | Calculated Property |
| γ | 0.02 | N/m | 514.68 | Calculated Property |
| γ | 0.01 | N/m | 566.05 | Calculated Property |
| γ | 0.01 | N/m | 617.42 | Calculated Property |
| γ | 0.00 | N/m | 668.78 | Calculated Property |
| γ | 0.00 | N/m | 720.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.02; 0.07] | W/m×K | [478.60; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 2.34760e-04 | |||
| Coefficient B | 8.63900e-01 | |||
| Coefficient C | 1.87800e+02 | |||
| Coefficient D | 1.93840e+05 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 478.60 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.02 | W/m×K | 478.60 | Calculated Property |
| λ | 0.03 | W/m×K | 536.53 | Calculated Property |
| λ | 0.03 | W/m×K | 594.47 | Calculated Property |
| λ | 0.04 | W/m×K | 652.40 | Calculated Property |
| λ | 0.04 | W/m×K | 710.33 | Calculated Property |
| λ | 0.05 | W/m×K | 768.27 | Calculated Property |
| λ | 0.05 | W/m×K | 826.20 | Calculated Property |
| λ | 0.06 | W/m×K | 884.13 | Calculated Property |
| λ | 0.06 | W/m×K | 942.07 | Calculated Property |
| λ | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.15] | W/m×K | [257.85; 478.60] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.78470e-01 | |||
| Coefficient B | -6.58430e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 100, LiquidThermalConductivity | |||
| Temperature range, min. | 257.85 | |||
| Temperature range, max. | 478.60 | |||
| λ | 0.16 | W/m×K | 257.85 | Calculated Property |
| λ | 0.16 | W/m×K | 282.38 | Calculated Property |
| λ | 0.16 | W/m×K | 306.91 | Calculated Property |
| λ | 0.16 | W/m×K | 331.43 | Calculated Property |
| λ | 0.16 | W/m×K | 355.96 | Calculated Property |
| λ | 0.15 | W/m×K | 380.49 | Calculated Property |
| λ | 0.15 | W/m×K | 405.02 | Calculated Property |
| λ | 0.15 | W/m×K | 429.54 | Calculated Property |
| λ | 0.15 | W/m×K | 454.07 | Calculated Property |
| λ | 0.15 | W/m×K | 478.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzyl alcohol.
Mixtures
- Benzyl alcohol + Ethanol, 2-methoxy-
- Benzyl alcohol + Ethanol, 2-ethoxy-
- Ethanol, 2-butoxy- + Benzyl alcohol
- Benzyl alcohol + Thymol
- Furfural + Benzyl alcohol + Water
- Aniline + Benzyl alcohol
- Aniline, N-methyl- + Benzyl alcohol
- Benzyl alcohol + Benzenamine, N,N-dimethyl-
- Benzyl alcohol + o-Chloroaniline
- Benzyl alcohol + m-Chloroaniline
- Benzyl alcohol + Acetic acid ethenyl ester
- Benzyl alcohol + Ethyl Acetate
- Benzyl alcohol + Acetic acid, 1,1-dimethylethyl ester
- Benzoic acid + Benzyl alcohol + Benzaldehyde
- Benzoic acid + Benzyl alcohol
- 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-
Find more mixtures with Benzyl alcohol.
Sources
- KDB Vapor Pressure Data
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Ionic liquid structural effects on solute partitioning in biphasic ionic liquid and supercritical carbon dioxide systems
- 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
- Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
- (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
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.