- InChI
- InChI=1S/C8H18O/c1-2-3-4-5-6-7-8-9/h9H,2-8H2,1H3
- InChI Key
- KBPLFHHGFOOTCA-UHFFFAOYSA-N
- Formula
- C8H18O
- SMILES
- CCCCCCCCO
- Molecular Weight1
- 130.23
- CAS
- 111-87-5
- Other Names
-
- 1-Hydroxyoctane
- 1-Octyl alcohol
- Alcohol C-8
- Alfol 8
- Dytol M-83
- Emery 3322
- Emery 3324
- Epal 8
- Heptyl carbinol
- Lorol 20
- Lorol C 8-98
- NSC 9823
- Octanol-(1)
- Octilin
- Octyl alcohol, normal-primary
- Prim-n-octyl alcohol
- Primary octyl alcohol
- Sipol L8
- capryl alcohol
- caprylic alcohol
- n-Heptyl carbinol
- n-Octan-1-ol
- n-Octanol
- n-octyl alcohol
- octan-1-ol
- octanol
- octyl alcohol
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- αp : Isobaric thermal expansion coefficient (1/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).
- εr : Dielectric Constant (Relative permittivity).
- Tflash,cc : Flash Point (Closed 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).
- ΔsubH° : Enthalpy of sublimation at standard conditions (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.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : 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.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.5697; 0.5963] |
|
|
| ω | 0.5963 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5697 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.5870 | KDB | |
| PAff | 799.00 | kJ/mol | NIST |
| ΔcH°liquid | [-5295.50; -5285.60] | kJ/mol |
|
| ΔcH°liquid | -5294.00 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -5295.50 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -5285.70 ± 2.70 | kJ/mol | NIST |
| ΔcH°liquid | -5285.60 | kJ/mol | NIST |
| μ | [1.65; 2.00] | debye |
|
| μ | 1.65 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 2.00 | debye | KDB |
| η | [0.0071430; 0.0075080] | Pa×s |
|
| η | 0.0075080 | Pa×s | Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties |
| η | 0.0071430 | Pa×s | 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 |
| εr | 10.34 | NCMS SOLV-DB | |
| Tflash,cc | 354.15 | K | NCMS SOLV-DB |
| ΔfG° | [-120.20; -117.00] | kJ/mol |
|
| ΔfG° | -117.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -120.20 | kJ/mol | KDB |
| ΔfH°gas | [-362.20; -354.10] | kJ/mol |
|
| ΔfH°gas | -357.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -360.10 | kJ/mol | KDB |
| ΔfH°gas | -355.50 | kJ/mol | NIST |
| ΔfH°gas | -355.60 ± 0.70 | kJ/mol | NIST |
| ΔfH°gas | -356.90 ± 1.30 | kJ/mol | NIST |
| ΔfH°gas | -354.10 | kJ/mol | NIST |
| ΔfH°gas | -354.20 ± 1.20 | kJ/mol | NIST |
| ΔfH°gas | -362.20 ± 3.10 | kJ/mol | NIST |
| ΔfH°liquid | [-435.00; -425.20] | kJ/mol |
|
| ΔfH°liquid | -426.60 ± 0.60 | kJ/mol | NIST |
| ΔfH°liquid | -428.00 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -425.20 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -435.00 ± 2.70 | kJ/mol | NIST |
| ΔfusH° | [23.70; 25.14] | kJ/mol |
|
| ΔfusH° | 25.14 | kJ/mol | Heat Capacities and Derived Thermodynamic Functions of 1-Hexanol, 1-Heptanol, 1-Octanol, and 1-Decanol between 5 K and 390 K |
| ΔfusH° | 23.70 | kJ/mol | Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol) |
| ΔsubH° | 100.40 | kJ/mol | NIST |
| ΔvapH° | [69.30; 72.80] | kJ/mol |
|
| ΔvapH° | 70.96 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 70.98 | kJ/mol | NIST |
| ΔvapH° | 69.30 | kJ/mol | NIST |
| ΔvapH° | 70.10 | kJ/mol | NIST |
| ΔvapH° | 71.60 | kJ/mol | NIST |
| ΔvapH° | 70.98 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 71.00 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 71.10 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 71.10 | kJ/mol | NIST |
| ΔvapH° | 72.80 ± 1.70 | kJ/mol | NIST |
| ΔvapH° | 72.80 | kJ/mol | NIST |
| IE | 9.94 | eV | Relay (1.0) Calculated Property |
| log10WS | [-2.39; -2.39] |
|
|
| log10WS | -2.39 | Aq. Solubility Prediction | |
| log10WS | -2.39 | Estimated Solubility | |
| logPoct/wat | 2.970 | NCMS SOLV-DB | |
| McVol | 129.450 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=2); %!d(float64=2)] |
|
|
| NFPA Fire | 2 | KDB | |
| NFPA Fire | 2 | NCMS SOLV-DB | |
| NFPA Health | [%!d(float64=1); %!d(float64=1)] |
|
|
| NFPA Health | 1 | KDB | |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [1777.00; 2860.41] | kPa |
|
| Pc | 2777.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Pc | 2860.41 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2783.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2777.00 | kPa | KDB |
| Pc | 2780.00 ± 30.00 | kPa | NIST |
| Pc | 2850.00 ± 50.00 | kPa | NIST |
| Pc | Outlier 1777.00 ± 20.00 | kPa | NIST |
| Pc | 2777.00 ± 20.00 | kPa | NIST |
| Pc | 2860.00 | kPa | NIST |
| Pc | 2860.00 | kPa | NIST |
| Ptriple | 9.60e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | [256.55; 265.66] | kg/m3 |
|
| ρc | 261.76 ± 3.91 | kg/m3 | NIST |
| ρc | 265.66 | kg/m3 | NIST |
| ρc | 256.55 ± 6.51 | kg/m3 | NIST |
| ρc | 265.66 ± 2.60 | kg/m3 | NIST |
| Inp | [175.63; 1095.00] |
|
|
| Inp | 1051.43 | NIST | |
| Inp | 1051.79 | NIST | |
| Inp | 1052.54 | NIST | |
| Inp | 1052.35 | NIST | |
| Inp | 1060.90 | NIST | |
| Inp | 1060.50 | NIST | |
| Inp | 1059.90 | NIST | |
| Inp | 1059.70 | NIST | |
| Inp | 1060.90 | NIST | |
| Inp | 1060.50 | NIST | |
| Inp | 1059.90 | NIST | |
| Inp | 1059.70 | NIST | |
| Inp | 1052.99 | NIST | |
| Inp | 1055.41 | NIST | |
| Inp | 1053.90 | NIST | |
| Inp | 1034.80 | NIST | |
| Inp | 1042.30 | NIST | |
| Inp | 1051.70 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1093.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1070.60 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1066.90 | NIST | |
| Inp | 1066.90 | NIST | |
| Inp | 1066.50 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1053.20 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1068.70 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1055.40 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1061.70 | NIST | |
| Inp | 1061.70 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1080.10 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1056.80 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1068.34 | NIST | |
| Inp | 1095.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1054.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1069.70 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1087.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1079.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1058.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | Outlier 175.63 | NIST | |
| Inp | Outlier 177.62 | NIST | |
| Inp | Outlier 176.31 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1076.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1082.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1068.34 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1084.00 | NIST | |
| Inp | 1081.00 | NIST | |
| Ip | [1507.00; 1605.00] |
|
|
| Ip | 1559.00 | NIST | |
| Ip | Outlier 1517.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1555.68 | NIST | |
| Ip | 1554.38 | NIST | |
| Ip | 1553.35 | NIST | |
| Ip | 1556.05 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1547.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | Outlier 1518.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1526.00 | NIST | |
| Ip | 1547.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1547.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1523.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1521.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1569.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | Outlier 1507.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1545.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1569.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1544.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1584.00 | NIST | |
| Ip | 1544.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | 1544.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | Outlier 1589.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1578.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1537.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | 1579.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1544.00 | NIST | |
| Ip | 1526.00 | NIST | |
| Ip | 1533.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1547.00 | NIST | |
| Ip | 1576.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1574.00 | NIST | |
| Ip | 1576.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1584.40 | NIST | |
| Ip | 1584.40 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1548.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1572.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1542.00 | NIST | |
| Ip | Outlier 1594.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | Outlier 1515.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1528.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1572.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1541.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1547.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | Outlier 1510.00 | NIST | |
| Ip | 1552.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1560.00 | NIST | |
| Ip | 1569.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | Outlier 1507.00 | NIST | |
| Ip | 1531.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1575.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | Outlier 1516.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | Outlier 1516.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1570.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | 1548.00 | NIST | |
| Ip | Outlier 1605.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1574.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1563.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1536.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1539.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1551.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1548.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | Outlier 1507.00 | NIST | |
| Ip | 1554.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | Outlier 1513.00 | NIST | |
| Ip | 1565.00 | NIST | |
| Ip | 1566.00 | NIST | |
| Ip | 1549.00 | NIST | |
| Ip | 1553.00 | NIST | |
| Ip | 1550.00 | NIST | |
| Ip | 1556.00 | NIST | |
| Ip | 1572.00 | NIST | |
| Ip | Outlier 1594.00 | NIST | |
| Ip | 1567.00 | NIST | |
| Ip | 1558.00 | NIST | |
| Ip | 1555.00 | NIST | |
| Ip | 1543.00 | NIST | |
| Ip | 1562.00 | NIST | |
| Ip | 1564.00 | NIST | |
| Ip | 1540.00 | NIST | |
| Ip | Outlier 1507.00 | NIST | |
| Ip | 1534.00 | NIST | |
| Ip | 1568.00 | NIST | |
| Ip | Outlier 1516.00 | NIST | |
| Ip | 1530.00 | NIST | |
| Ip | 1526.00 | NIST | |
| Ip | 1561.00 | NIST | |
| Ip | 1522.00 | NIST | |
| Ip | Outlier 1519.00 | NIST | |
| Ip | 1546.00 | NIST | |
| Ip | 1557.00 | NIST | |
| Ip | 1520.00 | NIST | |
| Ip | 1559.00 | NIST | |
| Ip | 1544.00 | NIST | |
| Ip | 1538.00 | NIST | |
| Ip | 1573.00 | NIST | |
| Tboil | [451.65; 469.20] | K |
|
| Tboil | 468.20 | K | Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data |
| Tboil | 466.00 | K | The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA |
| Tboil | 468.00 | K | (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems |
| Tboil | 468.00 | K | (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems |
| Tboil | 467.10 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 468.31 | K | KDB |
| Tboil | 467.15 | K | NCMS SOLV-DB |
| Tboil | 467.85 ± 0.60 | K | NIST |
| Tboil | 469.20 | K | NIST |
| Tboil | 467.60 | K | NIST |
| Tboil | 468.35 ± 0.50 | K | NIST |
| Tboil | 468.15 ± 1.00 | K | NIST |
| Tboil | 468.00 ± 2.00 | K | NIST |
| Tboil | 468.15 ± 1.00 | K | NIST |
| Tboil | 468.15 ± 1.00 | K | NIST |
| Tboil | 467.35 ± 1.00 | K | NIST |
| Tboil | 468.15 ± 0.50 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | 466.35 ± 1.00 | K | NIST |
| Tboil | 467.65 ± 1.00 | K | NIST |
| Tboil | 467.75 ± 1.00 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | 468.43 ± 0.20 | K | NIST |
| Tboil | 469.15 ± 2.00 | K | NIST |
| Tboil | 467.65 ± 1.00 | K | NIST |
| Tboil | 468.35 ± 0.25 | K | NIST |
| Tboil | 468.15 ± 3.90 | K | NIST |
| Tboil | 467.65 ± 2.00 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | 467.65 ± 0.40 | K | NIST |
| Tboil | 467.85 ± 0.50 | K | NIST |
| Tboil | 467.60 ± 0.50 | K | NIST |
| Tboil | 469.15 ± 3.00 | K | NIST |
| Tboil | 468.30 ± 0.30 | K | NIST |
| Tboil | 468.30 ± 0.50 | K | NIST |
| Tboil | 468.30 ± 0.50 | K | NIST |
| Tboil | 468.30 ± 1.00 | K | NIST |
| Tboil | 467.20 ± 0.40 | K | NIST |
| Tboil | 468.15 ± 2.00 | K | NIST |
| Tboil | Outlier 452.65 ± 3.00 | K | NIST |
| Tboil | 468.65 ± 1.00 | K | NIST |
| Tboil | 469.05 ± 1.00 | K | NIST |
| Tboil | 467.30 ± 2.00 | K | NIST |
| Tboil | Outlier 451.65 ± 1.50 | K | NIST |
| Tboil | 468.40 ± 3.00 | K | NIST |
| Tboil | 468.65 ± 3.00 | K | NIST |
| Tboil | 468.65 ± 1.00 | K | NIST |
| Tboil | 464.15 ± 3.00 | K | NIST |
| Tc | [650.56; 668.00] | K |
|
| Tc | 652.50 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Tc | 652.50 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 652.30 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 652.50 | K | KDB |
| Tc | 652.50 ± 0.50 | K | NIST |
| Tc | 652.20 ± 0.80 | K | NIST |
| Tc | 652.40 ± 0.60 | K | NIST |
| Tc | 652.40 ± 0.60 | K | NIST |
| Tc | 652.60 | K | NIST |
| Tc | 650.56 ± 0.30 | K | NIST |
| Tc | 652.50 | K | NIST |
| Tc | Outlier 668.00 ± 2.00 | K | NIST |
| Tc | 657.80 | K | NIST |
| Tc | 658.60 | K | NIST |
| Tfus | [256.20; 259.15] | K |
|
| Tfus | 257.70 | K | SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum |
| Tfus | 258.20 | K | Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents |
| Tfus | 258.03 | K | Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures |
| Tfus | 259.15 | K | Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water) |
| Tfus | 257.85 | K | Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum |
| Tfus | 257.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 257.65 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 257.60 | K | KDB |
| Tfus | 257.65 | K | Aq. Solubility Prediction |
| Tfus | 258.18 | K | NCMS SOLV-DB |
| Tfus | 258.35 ± 0.05 | K | NIST |
| Tfus | 258.03 ± 0.08 | K | NIST |
| Tfus | 256.20 ± 0.50 | K | NIST |
| Tfus | 256.25 ± 0.40 | K | NIST |
| Tfus | 256.40 ± 0.50 | K | NIST |
| Tfus | 256.90 ± 0.40 | K | NIST |
| Ttriple | 257.65 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 5.83 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.62 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.490; 0.509] | m3/kmol |
|
| Vc | 0.497 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value |
| Vc | 0.490 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.509 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.497 | m3/kmol | KDB |
| Vc | 0.497 | m3/kmol | NIST |
| Zc | [0.2540000; 0.2610000] |
|
|
| Zc | 0.2540000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 Compiled value | |
| Zc | 0.2610000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2543990 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 371.20 | K | 2.50 | NIST |
Datasets
Isobaric coefficient of expansion, 1/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Isobaric coefficient of expansion, 1/K - Liquid |
| 278.15 | 5000.00 | 0.0008 |
| 278.15 | 10000.00 | 0.0008 |
| 278.15 | 15000.00 | 0.0008 |
| 278.15 | 20000.00 | 0.0008 |
| 278.15 | 25000.00 | 0.0007 |
| 278.15 | 30000.00 | 0.0007 |
| 278.15 | 35000.00 | 0.0007 |
| 278.15 | 40000.00 | 0.0007 |
| 278.15 | 45000.00 | 0.0007 |
| 278.15 | 50000.00 | 0.0007 |
| 278.15 | 55000.00 | 0.0007 |
| 288.15 | 5000.00 | 0.0008 |
| 288.15 | 10000.00 | 0.0008 |
| 288.15 | 15000.00 | 0.0008 |
| 288.15 | 20000.00 | 0.0008 |
| 288.15 | 25000.00 | 0.0007 |
| 288.15 | 30000.00 | 0.0007 |
| 288.15 | 35000.00 | 0.0007 |
| 288.15 | 40000.00 | 0.0007 |
| 288.15 | 45000.00 | 0.0007 |
| 288.15 | 50000.00 | 0.0007 |
| 288.15 | 55000.00 | 0.0007 |
| 298.15 | 5000.00 | 0.0008 |
| 298.15 | 10000.00 | 0.0008 |
| 298.15 | 15000.00 | 0.0008 |
| 298.15 | 20000.00 | 0.0008 |
| 298.15 | 25000.00 | 0.0007 |
| 298.15 | 30000.00 | 0.0007 |
| 298.15 | 35000.00 | 0.0007 |
| 298.15 | 40000.00 | 0.0007 |
| 298.15 | 45000.00 | 0.0007 |
| 298.15 | 50000.00 | 0.0007 |
| 298.15 | 55000.00 | 0.0007 |
| 308.15 | 5000.00 | 0.0008 |
| 308.15 | 10000.00 | 0.0008 |
| 308.15 | 15000.00 | 0.0008 |
| 308.15 | 20000.00 | 0.0008 |
| 308.15 | 25000.00 | 0.0008 |
| 308.15 | 30000.00 | 0.0007 |
| 308.15 | 35000.00 | 0.0007 |
| 308.15 | 40000.00 | 0.0007 |
| 308.15 | 45000.00 | 0.0007 |
| 308.15 | 50000.00 | 0.0007 |
| 308.15 | 55000.00 | 0.0007 |
| 318.15 | 5000.00 | 0.0009 |
| 318.15 | 10000.00 | 0.0008 |
| 318.15 | 15000.00 | 0.0008 |
| 318.15 | 20000.00 | 0.0008 |
| 318.15 | 25000.00 | 0.0008 |
| 318.15 | 30000.00 | 0.0008 |
| 318.15 | 35000.00 | 0.0007 |
| 318.15 | 40000.00 | 0.0007 |
| 318.15 | 45000.00 | 0.0007 |
| 318.15 | 50000.00 | 0.0007 |
| 318.15 | 55000.00 | 0.0007 |
| 328.15 | 5000.00 | 0.0009 |
| 328.15 | 10000.00 | 0.0008 |
| 328.15 | 15000.00 | 0.0008 |
| 328.15 | 20000.00 | 0.0008 |
| 328.15 | 25000.00 | 0.0008 |
| 328.15 | 30000.00 | 0.0008 |
| 328.15 | 35000.00 | 0.0008 |
| 328.15 | 40000.00 | 0.0007 |
| 328.15 | 45000.00 | 0.0007 |
| 328.15 | 50000.00 | 0.0007 |
| 328.15 | 55000.00 | 0.0007 |
| 338.15 | 5000.00 | 0.0009 |
| 338.15 | 10000.00 | 0.0009 |
| 338.15 | 15000.00 | 0.0008 |
| 338.15 | 20000.00 | 0.0008 |
| 338.15 | 25000.00 | 0.0008 |
| 338.15 | 30000.00 | 0.0008 |
| 338.15 | 35000.00 | 0.0008 |
| 338.15 | 40000.00 | 0.0007 |
| 338.15 | 45000.00 | 0.0007 |
| 338.15 | 50000.00 | 0.0007 |
| 338.15 | 55000.00 | 0.0007 |
| 348.15 | 5000.00 | 0.0009 |
| 348.15 | 10000.00 | 0.0009 |
| 348.15 | 15000.00 | 0.0009 |
| 348.15 | 20000.00 | 0.0008 |
| 348.15 | 25000.00 | 0.0008 |
| 348.15 | 30000.00 | 0.0008 |
| 348.15 | 35000.00 | 0.0008 |
| 348.15 | 40000.00 | 0.0008 |
| 348.15 | 45000.00 | 0.0007 |
| 348.15 | 50000.00 | 0.0007 |
| 348.15 | 55000.00 | 0.0007 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 821.4 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 278.15 | 100.00 | 835.2 |
| 278.15 | 1000.00 | 835.7 |
| 278.15 | 5000.00 | 838.0 |
| 278.15 | 10000.00 | 841.0 |
| 278.15 | 15000.00 | 843.7 |
| 278.15 | 20000.00 | 846.4 |
| 278.15 | 25000.00 | 849.0 |
| 278.15 | 30000.00 | 851.5 |
| 278.15 | 35000.00 | 854.0 |
| 278.15 | 40000.00 | 856.4 |
| 278.15 | 45000.00 | 858.8 |
| 278.15 | 50000.00 | 861.1 |
| 278.15 | 55000.00 | 863.4 |
| 278.15 | 60000.00 | 865.5 |
| 288.15 | 100.00 | 828.4 |
| 288.15 | 1000.00 | 829.0 |
| 288.15 | 5000.00 | 831.5 |
| 288.15 | 10000.00 | 834.4 |
| 288.15 | 15000.00 | 837.3 |
| 288.15 | 20000.00 | 840.1 |
| 288.15 | 25000.00 | 842.8 |
| 288.15 | 30000.00 | 845.5 |
| 288.15 | 35000.00 | 848.0 |
| 288.15 | 40000.00 | 850.5 |
| 288.15 | 45000.00 | 852.9 |
| 288.15 | 50000.00 | 855.3 |
| 288.15 | 55000.00 | 857.6 |
| 288.15 | 60000.00 | 859.8 |
| 298.15 | 100.00 | 821.4 |
| 298.15 | 1000.00 | 822.0 |
| 298.15 | 5000.00 | 824.6 |
| 298.15 | 10000.00 | 827.7 |
| 298.15 | 15000.00 | 830.7 |
| 298.15 | 20000.00 | 833.6 |
| 298.15 | 25000.00 | 836.4 |
| 298.15 | 30000.00 | 839.1 |
| 298.15 | 35000.00 | 841.8 |
| 298.15 | 40000.00 | 844.4 |
| 298.15 | 45000.00 | 846.9 |
| 298.15 | 50000.00 | 849.4 |
| 298.15 | 55000.00 | 851.7 |
| 298.15 | 60000.00 | 853.9 |
| 308.15 | 100.00 | 814.5 |
| 308.15 | 1000.00 | 815.1 |
| 308.15 | 5000.00 | 817.8 |
| 308.15 | 10000.00 | 821.1 |
| 308.15 | 15000.00 | 824.2 |
| 308.15 | 20000.00 | 827.2 |
| 308.15 | 25000.00 | 830.1 |
| 308.15 | 30000.00 | 833.0 |
| 308.15 | 35000.00 | 835.7 |
| 308.15 | 40000.00 | 838.4 |
| 308.15 | 45000.00 | 841.0 |
| 308.15 | 50000.00 | 843.5 |
| 308.15 | 55000.00 | 846.0 |
| 308.15 | 60000.00 | 848.2 |
| 318.15 | 100.00 | 807.5 |
| 318.15 | 1000.00 | 808.1 |
| 318.15 | 5000.00 | 811.0 |
| 318.15 | 10000.00 | 814.4 |
| 318.15 | 15000.00 | 817.7 |
| 318.15 | 20000.00 | 820.8 |
| 318.15 | 25000.00 | 823.8 |
| 318.15 | 30000.00 | 826.8 |
| 318.15 | 35000.00 | 829.6 |
| 318.15 | 40000.00 | 832.4 |
| 318.15 | 45000.00 | 835.1 |
| 318.15 | 50000.00 | 837.7 |
| 318.15 | 55000.00 | 840.3 |
| 318.15 | 60000.00 | 842.6 |
| 328.15 | 100.00 | 800.4 |
| 328.15 | 1000.00 | 801.1 |
| 328.15 | 5000.00 | 804.1 |
| 328.15 | 10000.00 | 807.7 |
| 328.15 | 15000.00 | 811.1 |
| 328.15 | 20000.00 | 814.4 |
| 328.15 | 25000.00 | 817.5 |
| 328.15 | 30000.00 | 820.5 |
| 328.15 | 35000.00 | 823.5 |
| 328.15 | 40000.00 | 826.4 |
| 328.15 | 45000.00 | 829.1 |
| 328.15 | 50000.00 | 831.9 |
| 328.15 | 55000.00 | 834.5 |
| 328.15 | 60000.00 | 836.9 |
| 338.15 | 100.00 | 793.2 |
| 338.15 | 1000.00 | 793.9 |
| 338.15 | 5000.00 | 796.9 |
| 338.15 | 10000.00 | 800.8 |
| 338.15 | 15000.00 | 804.4 |
| 338.15 | 20000.00 | 807.8 |
| 338.15 | 25000.00 | 811.1 |
| 338.15 | 30000.00 | 814.2 |
| 338.15 | 35000.00 | 817.3 |
| 338.15 | 40000.00 | 820.3 |
| 338.15 | 45000.00 | 823.1 |
| 338.15 | 50000.00 | 825.9 |
| 338.15 | 55000.00 | 828.7 |
| 338.15 | 60000.00 | 831.2 |
| 348.15 | 100.00 | 785.6 |
| 348.15 | 1000.00 | 786.4 |
| 348.15 | 5000.00 | 789.8 |
| 348.15 | 10000.00 | 793.6 |
| 348.15 | 15000.00 | 797.4 |
| 348.15 | 20000.00 | 801.0 |
| 348.15 | 25000.00 | 804.5 |
| 348.15 | 30000.00 | 807.8 |
| 348.15 | 35000.00 | 810.9 |
| 348.15 | 40000.00 | 814.0 |
| 348.15 | 45000.00 | 817.0 |
| 348.15 | 50000.00 | 819.9 |
| 348.15 | 55000.00 | 822.7 |
| 348.15 | 60000.00 | 825.5 |
| 358.15 | 100.00 | 778.0 |
| 358.15 | 1000.00 | 778.8 |
| 358.15 | 5000.00 | 782.3 |
| 358.15 | 10000.00 | 786.4 |
| 358.15 | 15000.00 | 790.4 |
| 358.15 | 20000.00 | 794.1 |
| 358.15 | 25000.00 | 797.7 |
| 358.15 | 30000.00 | 801.1 |
| 358.15 | 35000.00 | 804.5 |
| 358.15 | 40000.00 | 807.7 |
| 358.15 | 45000.00 | 810.8 |
| 358.15 | 50000.00 | 813.6 |
| 358.15 | 55000.00 | 816.7 |
| 358.15 | 60000.00 | 819.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 2000.00 | 823.6 |
| 298.15 | 4010.00 | 824.8 |
| 298.15 | 6000.00 | 826.0 |
| 298.15 | 8000.00 | 827.2 |
| 298.15 | 10000.00 | 828.4 |
| 298.15 | 13010.00 | 830.1 |
| 298.15 | 16010.00 | 831.8 |
| 298.15 | 18990.00 | 833.4 |
| 298.15 | 22010.00 | 835.0 |
| 298.15 | 25010.00 | 836.6 |
| 298.15 | 28010.00 | 838.3 |
| 298.15 | 30010.00 | 839.3 |
| 303.15 | 1990.00 | 819.4 |
| 303.15 | 3990.00 | 820.6 |
| 303.15 | 5980.00 | 821.9 |
| 303.16 | 7980.00 | 823.1 |
| 303.15 | 10010.00 | 824.4 |
| 303.16 | 13000.00 | 826.2 |
| 303.15 | 16020.00 | 827.9 |
| 303.15 | 19030.00 | 829.7 |
| 303.16 | 22010.00 | 831.3 |
| 303.15 | 25000.00 | 833.0 |
| 303.16 | 28000.00 | 834.6 |
| 303.15 | 29980.00 | 835.6 |
| 313.15 | 1970.00 | 812.3 |
| 313.15 | 4000.00 | 813.6 |
| 313.15 | 6010.00 | 815.0 |
| 313.15 | 8000.00 | 816.3 |
| 313.15 | 10010.00 | 817.5 |
| 313.15 | 13030.00 | 819.4 |
| 313.15 | 15980.00 | 821.2 |
| 313.15 | 18990.00 | 823.0 |
| 313.15 | 21990.00 | 824.8 |
| 313.15 | 25000.00 | 826.5 |
| 313.15 | 27980.00 | 828.2 |
| 313.15 | 29990.00 | 829.3 |
| 323.15 | 2010.00 | 805.6 |
| 323.15 | 4010.00 | 807.0 |
| 323.15 | 6010.00 | 808.4 |
| 323.15 | 8000.00 | 809.7 |
| 323.15 | 10010.00 | 811.1 |
| 323.15 | 13020.00 | 813.0 |
| 323.15 | 16020.00 | 814.9 |
| 323.15 | 19010.00 | 816.8 |
| 323.15 | 22000.00 | 818.6 |
| 323.15 | 25010.00 | 820.4 |
| 323.15 | 28010.00 | 822.1 |
| 323.15 | 30020.00 | 823.3 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 821.4 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.14 | 1004.00 | 811.26 |
| 313.14 | 2019.00 | 811.95 |
| 313.14 | 3000.00 | 812.59 |
| 313.14 | 4020.00 | 813.22 |
| 313.14 | 4995.00 | 813.89 |
| 313.14 | 6000.00 | 814.53 |
| 313.14 | 7007.00 | 815.21 |
| 313.14 | 8012.00 | 815.83 |
| 313.14 | 8994.00 | 816.51 |
| 313.14 | 10014.00 | 817.19 |
| 313.14 | 11007.00 | 817.79 |
| 313.14 | 12000.00 | 818.42 |
| 313.14 | 12997.00 | 819.05 |
| 313.14 | 14001.00 | 819.67 |
| 313.14 | 14997.00 | 820.27 |
| 313.14 | 16002.00 | 820.89 |
| 313.14 | 17001.00 | 821.48 |
| 313.14 | 17997.00 | 822.1 |
| 313.14 | 19004.00 | 822.69 |
| 313.14 | 20007.00 | 823.28 |
| 313.14 | 21004.00 | 823.86 |
| 323.09 | 1007.00 | 804.26 |
| 323.09 | 2016.00 | 804.97 |
| 323.09 | 3019.00 | 805.7 |
| 323.09 | 4025.00 | 806.4 |
| 323.09 | 5012.00 | 807.07 |
| 323.09 | 6093.00 | 807.82 |
| 323.09 | 7143.00 | 808.56 |
| 323.09 | 8009.00 | 809.12 |
| 323.09 | 8989.00 | 809.77 |
| 323.09 | 10014.00 | 810.47 |
| 323.09 | 11031.00 | 811.14 |
| 323.09 | 12010.00 | 811.82 |
| 323.09 | 13005.00 | 812.44 |
| 323.09 | 14003.00 | 813.11 |
| 323.09 | 15012.00 | 813.76 |
| 323.09 | 16009.00 | 814.4 |
| 323.09 | 17005.00 | 815.04 |
| 323.09 | 18013.00 | 815.66 |
| 323.09 | 19003.00 | 816.26 |
| 323.09 | 20025.00 | 816.9 |
| 323.09 | 21081.00 | 817.56 |
| 323.09 | 22009.00 | 818.09 |
| 333.05 | 1038.00 | 797.31 |
| 333.05 | 2029.00 | 798.03 |
| 333.05 | 2999.00 | 798.76 |
| 333.05 | 4033.00 | 799.51 |
| 333.05 | 5020.00 | 800.25 |
| 333.05 | 6014.00 | 800.97 |
| 333.05 | 7029.00 | 801.69 |
| 333.05 | 8011.00 | 802.44 |
| 333.05 | 9005.00 | 803.11 |
| 333.05 | 10022.00 | 803.83 |
| 333.05 | 11011.00 | 804.55 |
| 333.05 | 12021.00 | 805.23 |
| 333.05 | 13022.00 | 805.92 |
| 333.05 | 14031.00 | 806.61 |
| 333.05 | 15010.00 | 807.28 |
| 333.05 | 16023.00 | 807.92 |
| 333.05 | 17012.00 | 808.59 |
| 333.05 | 18035.00 | 809.23 |
| 333.05 | 19009.00 | 809.87 |
| 333.05 | 20002.00 | 810.51 |
| 333.05 | 21011.00 | 811.15 |
| 333.05 | 22019.00 | 811.82 |
| 343.03 | 1049.00 | 790.6 |
| 343.03 | 2003.00 | 791.16 |
| 343.03 | 2981.00 | 791.93 |
| 343.03 | 4017.00 | 792.68 |
| 343.03 | 5000.00 | 793.37 |
| 343.03 | 6005.00 | 794.05 |
| 343.03 | 7018.00 | 794.88 |
| 343.03 | 8104.00 | 795.68 |
| 343.03 | 9014.00 | 796.44 |
| 343.03 | 10022.00 | 797.1 |
| 343.03 | 11028.00 | 797.87 |
| 343.03 | 11997.00 | 798.58 |
| 343.03 | 13030.00 | 799.3 |
| 343.03 | 14005.00 | 800.0 |
| 343.03 | 15002.00 | 800.66 |
| 343.03 | 16032.00 | 801.38 |
| 343.03 | 17016.00 | 801.99 |
| 343.03 | 18012.00 | 802.68 |
| 343.03 | 19005.00 | 803.29 |
| 343.03 | 20018.00 | 803.98 |
| 343.03 | 21014.00 | 804.61 |
| 343.03 | 22004.00 | 805.23 |
| 352.89 | 1023.00 | 782.71 |
| 352.89 | 2011.00 | 783.55 |
| 352.89 | 3032.00 | 784.42 |
| 352.89 | 4022.00 | 785.42 |
| 352.89 | 5005.00 | 786.18 |
| 352.89 | 6026.00 | 787.13 |
| 352.89 | 7003.00 | 787.9 |
| 352.89 | 8016.00 | 788.71 |
| 352.89 | 9007.00 | 789.47 |
| 352.89 | 10003.00 | 790.22 |
| 352.89 | 11022.00 | 791.0 |
| 352.89 | 12170.00 | 791.78 |
| 352.89 | 13015.00 | 792.51 |
| 352.89 | 14018.00 | 793.24 |
| 352.89 | 15009.00 | 794.0 |
| 352.89 | 16023.00 | 794.74 |
| 352.89 | 17010.00 | 795.48 |
| 352.89 | 18002.00 | 796.16 |
| 352.89 | 19029.00 | 796.9 |
| 352.89 | 20046.00 | 797.63 |
| 352.89 | 21023.00 | 798.3 |
| 362.77 | 1051.00 | 775.67 |
| 362.77 | 2025.00 | 776.41 |
| 362.77 | 3016.00 | 777.19 |
| 362.77 | 4009.00 | 778.05 |
| 362.77 | 4974.00 | 778.77 |
| 362.77 | 6005.00 | 779.51 |
| 362.77 | 7006.00 | 780.3 |
| 362.77 | 8011.00 | 780.95 |
| 362.77 | 9008.00 | 781.79 |
| 362.77 | 10034.00 | 782.62 |
| 362.77 | 11013.00 | 783.32 |
| 362.77 | 11987.00 | 784.03 |
| 362.77 | 13015.00 | 784.77 |
| 362.77 | 14006.00 | 785.51 |
| 362.77 | 14997.00 | 786.3 |
| 362.77 | 16001.00 | 787.03 |
| 362.77 | 17013.00 | 787.79 |
| 362.77 | 17997.00 | 788.55 |
| 362.77 | 19000.00 | 789.33 |
| 362.77 | 20023.00 | 790.04 |
| 362.77 | 21004.00 | 790.83 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 274.92 | 100.00 | 0.1580 |
| 274.85 | 5000.00 | 0.1598 |
| 274.82 | 10000.00 | 0.1611 |
| 274.77 | 20000.00 | 0.1639 |
| 274.63 | 30000.00 | 0.1669 |
| 294.93 | 100.00 | 0.1545 |
| 294.62 | 5000.00 | 0.1560 |
| 294.61 | 10100.00 | 0.1576 |
| 294.59 | 20100.00 | 0.1606 |
| 294.58 | 30000.00 | 0.1634 |
| 314.41 | 100.00 | 0.1511 |
| 314.95 | 5000.00 | 0.1530 |
| 314.91 | 10000.00 | 0.1545 |
| 314.86 | 20000.00 | 0.1578 |
| 314.86 | 30000.00 | 0.1609 |
| 334.98 | 100.00 | 0.1471 |
| 334.92 | 5000.00 | 0.1490 |
| 334.90 | 10000.00 | 0.1509 |
| 334.84 | 20000.00 | 0.1544 |
| 334.83 | 30000.00 | 0.1576 |
| 354.98 | 100.00 | 0.1427 |
| 354.41 | 5000.00 | 0.1445 |
| 354.36 | 10000.00 | 0.1466 |
| 354.50 | 20000.00 | 0.1505 |
| 354.35 | 30000.00 | 0.1539 |
| 374.96 | 100.00 | 0.1380 |
| 374.43 | 5100.00 | 0.1400 |
| 374.41 | 10000.00 | 0.1421 |
| 374.81 | 20000.00 | 0.1464 |
| 374.84 | 30000.00 | 0.1503 |
| 394.88 | 300.00 | 0.1325 |
| 395.13 | 5000.00 | 0.1349 |
| 395.05 | 10000.00 | 0.1377 |
| 394.82 | 20000.00 | 0.1420 |
| 394.85 | 30000.00 | 0.1461 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [198.32; 509.65] | J/mol×K | [298.15; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.38050e+02 | |||
| Coefficient B | 4.45900e+02 | |||
| Coefficient C | 1.57510e+03 | |||
| Coefficient D | 3.20160e+02 | |||
| Coefficient E | 7.18800e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 198.32 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 272.59 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 330.98 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 376.29 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 412.35 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 441.20 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 464.27 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 482.74 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 497.61 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 509.65 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [255.50; 415.66] | J/mol×K | [250.00; 467.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 5.71370e+02 | |||
| Coefficient B | -4.84900e+00 | |||
| Coefficient C | 1.97250e-02 | |||
| Coefficient D | -2.15320e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 250.00 | |||
| Temperature range, max. | 467.10 | |||
| Cp,liquid | 255.50 | J/mol×K | 250.00 | Calculated Property |
| Cp,liquid | 280.82 | J/mol×K | 274.12 | Calculated Property |
| Cp,liquid | 308.50 | J/mol×K | 298.24 | Calculated Property |
| Cp,liquid | 336.71 | J/mol×K | 322.37 | Calculated Property |
| Cp,liquid | 363.64 | J/mol×K | 346.49 | Calculated Property |
| Cp,liquid | 387.48 | J/mol×K | 370.61 | Calculated Property |
| Cp,liquid | 406.42 | J/mol×K | 394.73 | Calculated Property |
| Cp,liquid | 418.64 | J/mol×K | 418.86 | Calculated Property |
| Cp,liquid | 422.32 | J/mol×K | 442.98 | Calculated Property |
| Cp,liquid | 415.66 | J/mol×K | 467.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0147153; 0.0002902] | Pa×s | [280.00; 468.35] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -2.21280e-01 | |||
| Coefficient B | 3.01840e+03 | |||
| Coefficient C | -2.80540e+00 | |||
| Coefficient D | 1.31410e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 280.00 | |||
| Temperature range, max. | 468.35 | |||
| η | 0.0147153 | Pa×s | 280.00 | Calculated Property |
| η | 0.0066642 | Pa×s | 300.93 | Calculated Property |
| η | 0.0034117 | Pa×s | 321.86 | Calculated Property |
| η | 0.0019362 | Pa×s | 342.78 | Calculated Property |
| η | 0.0011997 | Pa×s | 363.71 | Calculated Property |
| η | 0.0008020 | Pa×s | 384.64 | Calculated Property |
| η | 0.0005730 | Pa×s | 405.57 | Calculated Property |
| η | 0.0004342 | Pa×s | 426.49 | Calculated Property |
| η | 0.0003467 | Pa×s | 447.42 | Calculated Property |
| η | 0.0002902 | Pa×s | 468.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [76.79; 0.00] | kJ/mol | [257.65; 652.30] |
ChemSep v8.3 pure component data Compiled value
|
| 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 | 7.24680e+01 | |||
| Coefficient B | -1.24640e+00 | |||
| Coefficient C | 3.67970e+00 | |||
| Coefficient D | -2.06650e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.52300e+02 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 652.30 | |||
| ΔvapH | 76.79 | kJ/mol | 257.65 | Calculated Property |
| ΔvapH | 71.89 | kJ/mol | 301.50 | Calculated Property |
| ΔvapH | 66.07 | kJ/mol | 345.35 | Calculated Property |
| ΔvapH | 59.70 | kJ/mol | 389.20 | Calculated Property |
| ΔvapH | 53.07 | kJ/mol | 433.05 | Calculated Property |
| ΔvapH | 46.41 | kJ/mol | 476.90 | Calculated Property |
| ΔvapH | 39.81 | kJ/mol | 520.75 | Calculated Property |
| ΔvapH | 33.11 | kJ/mol | 564.60 | Calculated Property |
| ΔvapH | 25.43 | kJ/mol | 608.45 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 652.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [358.71; 495.05] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.45038e+01 | |||
| Coefficient B | -3.54647e+03 | |||
| Coefficient C | -1.09245e+02 | |||
| Temperature range, min. | 358.71 | |||
| Temperature range, max. | 495.05 | |||
| Pvap | 1.33 | kPa | 358.71 | Calculated Property |
| Pvap | 3.01 | kPa | 373.86 | Calculated Property |
| Pvap | 6.22 | kPa | 389.01 | Calculated Property |
| Pvap | 11.92 | kPa | 404.16 | Calculated Property |
| Pvap | 21.45 | kPa | 419.31 | Calculated Property |
| Pvap | 36.55 | kPa | 434.45 | Calculated Property |
| Pvap | 59.38 | kPa | 449.60 | Calculated Property |
| Pvap | 92.58 | kPa | 464.75 | Calculated Property |
| Pvap | 139.18 | kPa | 479.90 | Calculated Property |
| Pvap | 202.64 | kPa | 495.05 | Calculated Property |
| Pvap | [9.60e-05; 2781.67] | kPa | [257.65; 652.30] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37202e+02 | |||
| Coefficient B | -1.36670e+04 | |||
| Coefficient C | -1.68260e+01 | |||
| Coefficient D | 9.36660e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 652.30 | |||
| Pvap | 9.60e-05 | kPa | 257.65 | Calculated Property |
| Pvap | 0.02 | kPa | 301.50 | Calculated Property |
| Pvap | 0.50 | kPa | 345.35 | Calculated Property |
| Pvap | 5.86 | kPa | 389.20 | Calculated Property |
| Pvap | 35.02 | kPa | 433.05 | Calculated Property |
| Pvap | 132.07 | kPa | 476.90 | Calculated Property |
| Pvap | 362.50 | kPa | 520.75 | Calculated Property |
| Pvap | 802.41 | kPa | 564.60 | Calculated Property |
| Pvap | 1549.15 | kPa | 608.45 | Calculated Property |
| Pvap | 2781.67 | kPa | 652.30 | Calculated Property |
| Pvap | [7.80e-05; 2692.59] | kPa | [257.65; 652.50] |
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 | 2.04801e+02 | |||
| Coefficient B | -1.63274e+04 | |||
| Coefficient C | -2.73260e+01 | |||
| Coefficient D | 1.22481e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 652.50 | |||
| Pvap | 7.80e-05 | kPa | 257.65 | Calculated Property |
| Pvap | 0.01 | kPa | 301.52 | Calculated Property |
| Pvap | 0.49 | kPa | 345.39 | Calculated Property |
| Pvap | 5.66 | kPa | 389.27 | Calculated Property |
| Pvap | 33.30 | kPa | 433.14 | Calculated Property |
| Pvap | 124.61 | kPa | 477.01 | Calculated Property |
| Pvap | 343.81 | kPa | 520.88 | Calculated Property |
| Pvap | 771.79 | kPa | 564.76 | Calculated Property |
| Pvap | 1508.48 | kPa | 608.63 | Calculated Property |
| Pvap | 2692.59 | kPa | 652.50 | Calculated Property |
| Pvap | [219.21; 606.90] | kPa | [502.19; 553.99] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37338e+01 | |||
| Coefficient B | -3.10910e+03 | |||
| Coefficient C | -1.29565e+02 | |||
| Reference | Ambrose, Sprake, et al., 1975 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 502.19 | |||
| Temperature range, max. | 553.99 | |||
| Pvap | 219.21 | kPa | 502.19 | Calculated Property |
| Pvap | 248.87 | kPa | 507.95 | Calculated Property |
| Pvap | 281.48 | kPa | 513.70 | Calculated Property |
| Pvap | 317.20 | kPa | 519.46 | Calculated Property |
| Pvap | 356.22 | kPa | 525.21 | Calculated Property |
| Pvap | 398.70 | kPa | 530.97 | Calculated Property |
| Pvap | 444.84 | kPa | 536.72 | Calculated Property |
| Pvap | 494.80 | kPa | 542.48 | Calculated Property |
| Pvap | 548.76 | kPa | 548.23 | Calculated Property |
| Pvap | 606.90 | kPa | 553.99 | Calculated Property |
| Pvap | [0.14; 5.25] | kPa | [328.02; 387.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.56786e+01 | |||
| Coefficient B | -4.03764e+03 | |||
| Coefficient C | -9.90000e+01 | |||
| Reference | Ambrose, Ellender, et al., 1974 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 328.02 | |||
| Temperature range, max. | 387.00 | |||
| Pvap | 0.14 | kPa | 328.02 | Calculated Property |
| Pvap | 0.23 | kPa | 334.57 | Calculated Property |
| Pvap | 0.37 | kPa | 341.13 | Calculated Property |
| Pvap | 0.57 | kPa | 347.68 | Calculated Property |
| Pvap | 0.87 | kPa | 354.23 | Calculated Property |
| Pvap | 1.29 | kPa | 360.79 | Calculated Property |
| Pvap | 1.88 | kPa | 367.34 | Calculated Property |
| Pvap | 2.69 | kPa | 373.89 | Calculated Property |
| Pvap | 3.79 | kPa | 380.45 | Calculated Property |
| Pvap | 5.25 | kPa | 387.00 | Calculated Property |
| Pvap | [5.05; 135.56] | kPa | [386.42; 479.27] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.35917e+01 | |||
| Coefficient B | -2.93409e+03 | |||
| Coefficient C | -1.41328e+02 | |||
| Reference | Ambrose and Sprake, 1970 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 386.42 | |||
| Temperature range, max. | 479.27 | |||
| Pvap | 5.05 | kPa | 386.42 | Calculated Property |
| Pvap | 8.20 | kPa | 396.74 | Calculated Property |
| Pvap | 12.81 | kPa | 407.05 | Calculated Property |
| Pvap | 19.35 | kPa | 417.37 | Calculated Property |
| Pvap | 28.37 | kPa | 427.69 | Calculated Property |
| Pvap | 40.52 | kPa | 438.00 | Calculated Property |
| Pvap | 56.49 | kPa | 448.32 | Calculated Property |
| Pvap | 77.08 | kPa | 458.64 | Calculated Property |
| Pvap | 103.13 | kPa | 468.95 | Calculated Property |
| Pvap | 135.56 | kPa | 479.27 | Calculated Property |
| Pvap | [0.72; 100.60] | kPa | [352.10; 468.50] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.32363e+01 | |||
| Coefficient B | -2.75536e+03 | |||
| Coefficient C | -1.49043e+02 | |||
| Reference | Kemme and Kreps, 1969 | |||
| Temperature range, min. | 352.10 | |||
| Temperature range, max. | 468.50 | |||
| Pvap | 0.72 | kPa | 352.10 | Calculated Property |
| Pvap | 1.62 | kPa | 365.03 | Calculated Property |
| Pvap | 3.32 | kPa | 377.97 | Calculated Property |
| Pvap | 6.32 | kPa | 390.90 | Calculated Property |
| Pvap | 11.27 | kPa | 403.83 | Calculated Property |
| Pvap | 19.00 | kPa | 416.77 | Calculated Property |
| Pvap | 30.53 | kPa | 429.70 | Calculated Property |
| Pvap | 47.05 | kPa | 442.63 | Calculated Property |
| Pvap | 69.91 | kPa | 455.57 | Calculated Property |
| Pvap | 100.60 | kPa | 468.50 | Calculated Property |
| Pvap | [6.55e-03; 0.83] | kPa | [293.00; 353.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.95186e+01 | |||
| Coefficient B | -5.99446e+03 | |||
| Coefficient C | -4.87990e+01 | |||
| Reference | Geiseler, Fruwert, et al., 1966 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 293.00 | |||
| Temperature range, max. | 353.00 | |||
| Pvap | 6.55e-03 | kPa | 293.00 | Calculated Property |
| Pvap | 0.01 | kPa | 299.67 | Calculated Property |
| Pvap | 0.02 | kPa | 306.33 | Calculated Property |
| Pvap | 0.04 | kPa | 313.00 | Calculated Property |
| Pvap | 0.07 | kPa | 319.67 | Calculated Property |
| Pvap | 0.12 | kPa | 326.33 | Calculated Property |
| Pvap | 0.21 | kPa | 333.00 | Calculated Property |
| Pvap | 0.34 | kPa | 339.67 | Calculated Property |
| Pvap | 0.53 | kPa | 346.33 | Calculated Property |
| Pvap | 0.83 | kPa | 353.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [856.09; 255.84] | kg/m3 | [257.65; 652.30] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.37844e+01 | |||
| Coefficient B | 2.49310e-01 | |||
| Coefficient C | 6.52300e+02 | |||
| Coefficient D | 2.78240e-01 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 652.30 | |||
| ρl | 856.09 | kg/m3 | 257.65 | Calculated Property |
| ρl | 823.39 | kg/m3 | 301.50 | Calculated Property |
| ρl | 789.03 | kg/m3 | 345.35 | Calculated Property |
| ρl | 752.59 | kg/m3 | 389.20 | Calculated Property |
| ρl | 713.48 | kg/m3 | 433.05 | Calculated Property |
| ρl | 670.76 | kg/m3 | 476.90 | Calculated Property |
| ρl | 622.83 | kg/m3 | 520.75 | Calculated Property |
| ρl | 566.43 | kg/m3 | 564.60 | Calculated Property |
| ρl | 492.72 | kg/m3 | 608.45 | Calculated Property |
| ρl | 255.84 | kg/m3 | 652.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.01] | N/m | [257.65; 468.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.08054e-02 | |||
| Coefficient B | -7.95000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 468.15 | |||
| γ | 0.03 | N/m | 257.65 | Calculated Property |
| γ | 0.03 | N/m | 281.04 | Calculated Property |
| γ | 0.03 | N/m | 304.43 | Calculated Property |
| γ | 0.02 | N/m | 327.82 | Calculated Property |
| γ | 0.02 | N/m | 351.21 | Calculated Property |
| γ | 0.02 | N/m | 374.59 | Calculated Property |
| γ | 0.02 | N/m | 397.98 | Calculated Property |
| γ | 0.02 | N/m | 421.37 | Calculated Property |
| γ | 0.02 | N/m | 444.76 | Calculated Property |
| γ | 0.01 | N/m | 468.15 | Calculated Property |
| γ | [0.03; 0.00] | N/m | [257.65; 652.30] |
ChemSep v8.3 pure component data Compiled value
|
| 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 | 5.13950e-02 | |||
| Coefficient B | 1.04830e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.52300e+02 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 652.30 | |||
| γ | 0.03 | N/m | 257.65 | Calculated Property |
| γ | 0.03 | N/m | 301.50 | Calculated Property |
| γ | 0.02 | N/m | 345.35 | Calculated Property |
| γ | 0.02 | N/m | 389.20 | Calculated Property |
| γ | 0.02 | N/m | 433.05 | Calculated Property |
| γ | 0.01 | N/m | 476.90 | Calculated Property |
| γ | 0.01 | N/m | 520.75 | Calculated Property |
| γ | 0.01 | N/m | 564.60 | Calculated Property |
| γ | 0.00 | N/m | 608.45 | Calculated Property |
| γ | 0.00 | N/m | 652.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.10] | W/m×K | [468.35; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | -3.02380e-03 | |||
| Coefficient B | 8.74500e-01 | |||
| Coefficient C | -1.33520e+04 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 468.35 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 468.35 | Calculated Property |
| λgas | 0.03 | W/m×K | 527.42 | Calculated Property |
| λgas | 0.04 | W/m×K | 586.49 | Calculated Property |
| λgas | 0.04 | W/m×K | 645.57 | Calculated Property |
| λgas | 0.05 | W/m×K | 704.64 | Calculated Property |
| λgas | 0.06 | W/m×K | 763.71 | Calculated Property |
| λgas | 0.07 | W/m×K | 822.78 | Calculated Property |
| λgas | 0.08 | W/m×K | 881.86 | Calculated Property |
| λgas | 0.09 | W/m×K | 940.93 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.17; 0.09] | W/m×K | [257.65; 570.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.35280e-01 | |||
| Coefficient B | -2.50000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 257.65 | |||
| Temperature range, max. | 570.15 | |||
| λliquid | 0.17 | W/m×K | 257.65 | Calculated Property |
| λliquid | 0.16 | W/m×K | 292.37 | Calculated Property |
| λliquid | 0.15 | W/m×K | 327.09 | Calculated Property |
| λliquid | 0.14 | W/m×K | 361.82 | Calculated Property |
| λliquid | 0.14 | W/m×K | 396.54 | Calculated Property |
| λliquid | 0.13 | W/m×K | 431.26 | Calculated Property |
| λliquid | 0.12 | W/m×K | 465.98 | Calculated Property |
| λliquid | 0.11 | W/m×K | 500.71 | Calculated Property |
| λliquid | 0.10 | W/m×K | 535.43 | Calculated Property |
| λliquid | 0.09 | W/m×K | 570.15 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Octanol.
Mixtures
- 1-Octanol + Benzoic acid, 2-(acetylamino)-
- 1-Octanol + Benzoic acid, 3-(acetylamino)-
- 1-Octanol + Acedoben
- Acetamide, N-(2-hydroxyphenyl)- + 1-Octanol
- Metacetamol + 1-Octanol
- Acetaminophen + 1-Octanol
- Benzamide, 2-hydroxy- + 1-Octanol
- 1-Octanol + 3-hydroxy-benzamide
- 1-Octanol + 4-Hydroxybenzamide
- 1-Octanol + Acetamide, N-phenyl-
- Benzoic acid + 1-Octanol
- Benzamide + 1-Octanol
- 1-Octanol + Phenol
- 1-Octanol + Propanoic acid + Water
- Toluene + 1-Octanol
- 1-Octene + 1-Octanol
- Dodecane + 1-Octanol
- Dodecane + Tri-n-butylphosphate + 1-Octanol
- 1-Octanol + Ethanol, 2-(2-butoxyethoxy)-
- Formamide, N,N-dimethyl- + 1-Octanol
Find more mixtures with 1-Octanol.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 4 ChEDL chemicals 1.5.2, from Gude, M.; Teja, A. S. Vapor-Liquid Critical Properties of Elements and Compounds. 4. Aliphatic Alkanols. J. Chem. Eng. Data 1995, 40, 1025-1036.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- 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.
- Speeds of Sound and Isentropic Compressibilities in Binary Mixtures of 2-Propanol with Several 1-Alkanols at 298.15K
- Excess Volumes, Densities, Speeds of Sound, and Viscosities for the Binary Systems of 1-Octanol with Hexadecane and Squalane at (298.15, 303.15 and 308.15) K
- Liquid phase behavior of imidazolium-based ionic liquids with alcohols: effect of hydrogen bonding and non-polar interactions
- Liquid-liquid equilibria for ternary systems of (water + carboxylic acid + 1-octanol) at 293.15 K: modeling phase equilibria using a solvatochromic approach
- Excess molar enthalpies for mixtures of carbon dioxide + a modifier (5 mol% methanol or 1-octanol) and hexane at 308.15K and 12.40MPa
- 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
- Solubility of naproxen in several organic solvents at different temperatures
- 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
- Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Benchmarks for the fifth industrial fluid properties simulation challenge
- 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}
- SLE and LLE for tri-butylphosphate or tri-octylamine contained systems; extractive solvents of Molybdenum
- Vapor pressure of selected aliphatic alcohols by ebulliometry. Part 1
- The solid-liquid phase diagrams of binary mixtures of even saturated fatty alcohols
- Liquid-liquid phase equilibrium of (piperidinium-based ionic liquid + an alcohol) binary systems and modelling with NRHB and PCP-SAFT
- Isobaric vapor-liquid equilibrium for binary systems containing benzothiophene
- Liquid phase equilibria of the system (water + phosphoric acid + 1-octanol) at T = (298.2, 308.2, and 318.2) K
- Solid-liquid equilibrium, excess molar volume, and deviations in the molar refractivity for the binary and ternary mixtures of Alamine 304-1 with 1-octanol, 2-octanol, and 1-decanol
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- Solubility and tie line data for the aqueous solutions of butyric acid with 1-octanol and 2-ethyl-1-hexanol at various temperatures
- Towards automated characterisation of liquid-liquid equilibria
- Unusual behavior of the isotope effect on miscibility of 1-hexyl-3-methylimidazolium bis(trifluorosulfonyl)imide with 1-alkanols
- Ternary phase diagrams for aqueous mixtures of butyric acid with several solvents: experimental and correlated data
- Modeling extraction equilibria of butyric acid distributed between water and tri-n-butyl amine/diluent or tri-n-butyl phosphate/diluent system: Extension of the LSER approach
- Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
- The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
- Solubility of pharmaceuticals in water and alcohols
- 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.
- Phase equilibrium for ternary liquid systems of water + di-(2- ethylhexyl)phosphoric acid + organic diluents: Thermodynamic study
- Determination and prediction of solubilities of active pharmaceutical ingredients in selected organic solvents
- Study of phase equilibria and the physicochemical properties of selected pharmaceuticals
- Aqueous solubility, vapor pressure and octanol-water partition coefficient of two phthalate isomers dibutyl phthalate and di-isobutyl phthalate contaminants of recycled food packages
- An experimental investigation on the solubility of methane in 1-octanol and n-dodecane at ambient temperatures
- Enhanced partition model of 4-nitrophenol in water - octanol system. Effects of association/dissociation processes
- Equilibrium data and GC-PC SAFT predictions for furanic extraction
- Effect of polarity and temperature on the binary interaction between D2EHPA extractant and organic solvents (kerosene, n-heptane, chlorobenzene and 1-octanol): Experimental and thermodynamics
- Solubility and dissolution characteristics of capecitabine in pure lower alcohols and water with methanol mixture solvents at atmospheric pressure and different temperatures
- Study of the physicochemical properties of protein kinase CK2 inhibitors -TBBt, TBBi and 2-Me-TBBi
- Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
- Isothermal (vapour + liquid) equilibrium at several temperatures of (1-chlorobutane + 1-octanol, or 1-decanol)
- 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
- (Liquid + liquid) equilibria of (water + propionic acid + alcohol) ternary systems
- 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
- Phase equilibria of didecyldimethylammonium nitrate ionic liquid with water and organic solvents
- Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
- Study of molecular interactions in binary liquid mixtures of 1-octanol with n-hexane, n-octane, and n-decane using volumetric, viscometric, and acoustic properties
- Thermodynamics of (1-alkanol + linear monoether) systems
- Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
- (Liquid + liquid) equilibria of (water + lactic acid + alcohol) ternary systems
- Molar excess enthalpies at T = 298.15 K for (1-alkanol + dibutylether) systems
- Isobaric thermal expansivity behaviour against temperature and pressure of associating fluids
- 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
- Partial molar volumes of some drug and pro-drug substances in 1-octanol at T = 298.15 K
- Solubility and pKa of select pharmaceuticals in water, ethanol, and 1-octanol
- Thermodynamic aspects of solubility, solvation and partitioning processes of some sulfonamides
- Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
- Enthalpy of cooperative hydrogen bonding in complexes of tertiary amines with aliphatic alcohols: Calorimetric study
- 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
- 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
- Partition coefficient n-octanol/water of propranolol and atenolol at different temperatures: Experimental and theoretical studies
- A thermodynamic study of solute solvent interactions through dielectric properties of the mixtures consisting of 1,4-butanediol, 1-octanol, and 1,4-dioxane at different temperatures
- Solubility of ionic liquids in water and octan-1-ol and octan-1-ol/water, or 2-phenylethanol/water partition coefficients
- Tie-line data for the aqueous solutions of phenol with organic solvents at T = 298.2 K
- Physico-chemical properties of binary mixtures of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol at different temperatures
- 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
- Thermodynamic, transport and excess properties of 2-butoxy ethanol +1-alkanol (C6,C8,C10) at different temperatures
- Temperature and concentration dependence of the relative permittivity of (1,3-butanediol + 1-octanol or 1,4-dioxane) binary liquid mixtures
- Thermodynamic aspects of solubility and partitioning processes of some sulfonamides in the solvents modeling biological media
- Volumetric and compressibility studies on tri-n-butyl phosphate (TBP)-phase modifier (1-octanol, 1-decanol and isodecanol) interactions from T = (298.15 to 323.15) K
- 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
- Effect of temperature and chain length on the viscosity and surface tension of binary systems of N,N-dimethylformamide with 1-octanol, 1-nonanol and 1-decanol
- The physicochemical properties and solubility of pharmaceuticals - Methyl xanthines
- Blood porphyrins in binary mixtures of N,N-dimethylformamide with 1-octanol and chloroform: The energetics of solvation, (solute + cosolvent) interactions and model calculations
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Thermodynamics of mixing for binary mixtures of 1-octanol and 1-decanol with n-dodecane and ternary mixture of (TBP + 1-octanol + dodecane) at T = (298.15 to 323.15) K
- Solution thermodynamics of pyrazinamide, isoniazid, and p-aminobenzoic acid in buffers and octanol
- Impact of structural modification of 1,2,4-thiadiazole derivatives on thermodynamics of solubility and solvation processes in 1-octanol and n-hexane
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- Studies on the importance of chain length of alkanols on the thermodynamic and transport properties of liquid mixtures at various temperatures
- Physico-chemical characterization antituberculosis thioacetazone: Vapor pressure, solubility and lipophilicity
- 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
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- A thermodynamic study of sublimation, dissolution and distribution processes of anti-inflammatory drug Clonixin
- Solubility and vapor pressure data of bioactive 6-(acetylamino)-N-(5-ethyl-1,3,4-thiadiazol-2-yl) hexanamide
- Thermodynamic study of aceclofenac solubility, distribution and sublimation
- Solution enthalpies of 1-bromoadamantane in monoalcohols at 298.15K
- Thermophysical properties and thermodynamic phase behavior of ionic liquids
- Excess molar enthalpies and heat capacities of dimethyl sulfoxide + seven normal alkanols at 303.15K and atmospheric pressure
- Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Measurement and Correlation for Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
- Solvation of the photodynamic therapy agent in the model lipid protein system: The evidence of porphyrin preferential solvation by apolar environment
- Vapor pressure of 1-octanol below 5 kPa using DSC
- Effect of chain length of alcohol on thermodynamic properties of their binary mixtures with benzylalcohol
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Thermogravimetric measurement of evaporation: Data analysis based on the Stefan tube
- Thermodynamics of mixtures containing amines. XVI. CE pm of 1-butanol, 1-octanol or 1-decanol + benzylamine systems at (298.15, 308.15, 318.15 and 333.15) K
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- The solubility of ethionamide and structural analogues in buffer solutions, octanol and hexane at several temperatures
- Isobaric phase equilibrium of morpholine + 1-decanol, volumetric properties and molar refractivity from 293.15 to 333.15 K of morpholine + 1-decanol and 1-octanol + toluene system with applications of Prigogine-Flory-Patterson theory
- On the photothermal characterization of liquid thermoelectrics. New methodology based on coupled pyroelectric-Seebeck effects, together with frequency and thickness scanning procedures
- Physico-chemical study of bioactive N-(5-ethyl-1,3,4-thiadiazole-2-yl)-4-nitrobenzamide: Sublimation, solubility and distribution
- Analysis of solute-pyridine intermolecular interactions based on experimental enthalpies of solution and enthalpies of solvation of solutes dissolved in pyridine
- Experimental solubility of clotrimazole and some thermodynamic aspects of dissolution in different solvents
- Thermodynamic and spectral studies of molecular interactions in binary liquid mixtures of 1-butoxy-2- propanol with 1-alcohols
- Solubility and distribution of salinazid and vanillin isoniazid in the solvents modeling biological media
- 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
- Ternary and Quaternary Liquid-Liquid Equilibria for Systems of Methyl Butyl Ketone + Water + Hydroquinone + Phenol at 313.2 K and Atmospheric Pressure
- Equilibrium Study on the Extraction of Levulinic Acid from Aqueous Solution with Aliquat 336 Dissolved in Different Diluents: Solvent s Polarity Effect and Column Design
- Effect of Temperature on Reactive Extraction of Gallic Acid Using Tri-n-butyl Phosphate, Tri-n-octylamine and Aliquat 336
- Sulfasalazine: Dissolution and Distribution in Pharmaceutically Relevant Mediums
- Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
- Measurement and Modeling of Solubility of para-tert-Butylbenzoic Acid in Pure and Mixed Organic Solvents at Different Temperatures
- L(+)-tartaric Acid Separations Using Aliquat 336 in n-Heptane, Kerosene, and 1-Octanol at 300 +- 1 K
- Extraction of Citric Acid and Maleic Acid from Their Aqueous Solutions Using a Phosphorus-Bonded Extractant, Tri-n-octylphosphineoxide, and a Secondary Amine, Dioctylamine
- Vapor Pressure and Isobaric Vapor-Liquid Equilibrium for Binary Systems of Furfural, 2-Acetylfuran, and 5-Methylfurfural at 3.60 and 5.18 kPa
- Thermodynamic Aspects of Solubility and Solvation of Bioactive Bicyclic Derivatives in Organic Solvents
- High-Pressure Phase Equilibria of Carbon Dioxide + 1-Octanol Binary System
- Physical Behavior of the Phases from the Liquid-Liquid Equilibrium of Citrus Essential Oils Systems at 298.2 K
- Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
- Correlation Studies of Cyclohexanone/(C5-C10) Alkan-1-ol Binary Mixtures: PC-SAFT Model and Free Volume Theory
- Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
- Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
- Liquid-Liquid Equilibrium for Ternary Systems of Water + 2,2,3,3-Tetrafluoro-1-propanol + Anisole/1-Octanol at 298.2, 308.2, and 318.2 K
- 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
- Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
- Viscosity and Density of n-Alcohols at Temperatures between (298.15 and 323.15) K and Pressures up to 30 MPa
- Experimental Study on Reactive Extraction of Malonic Acid with Validation by Fourier Transform Infrared Spectroscopy
- 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
- Thermodynamic Modeling of Triglycerides using PC-SAFT
- Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
- Kirkwood-Buff Integrals, Excess Volume, and Preferential Solvation in Pentanoic Acid/(C5-C10) 1-Alkanol Binary Mixtures
- Thermodynamic Studies of Solubility for Naphthalene in 12 Solvents from 279 to 330 K
- Parametric Analysis of Mandelic Acid Separation from Aqueous Solutions by Using Secondary Amine Mixture (Amberlite LA-2) in Various Diluents
- Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
- Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
- 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 and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
- Thermodynamic Properties of 1-Hexyl-3-methylimidazolium Nitrate and 1-Alkanols Mixtures: PC-SAFT Model
- Liquid-Liquid Equilibria for the Ternary and Quaternary Systems of Water + Trimethylolpropane + (2-Ethylhexan-1-ol/Octan-1-ol) + Formaldehyde at 298.15 K
- Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
- Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
- Excess molar volumes and enthalpies of mixing for the ternary system (butyl butyrate + 1-octanol + dodecane) at the temperature 308.15 K.
- Vapor Liquid Equilibrium between (278.15 and 323.15) K and Excess Functions at T ) 298.15 K for 1-Bromobutane with 1-Octanol or 1-Decanol
- Experimental Solid + Liquid Equilibria and Excess Molar Volume of Alkanol + Octylamine Mixtures. Analysis in Terms of ERAS, DISQUAC, and Modified UNIFAC
- 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
- Vapor Pressure Determination of the Aliphatic C5 to C8 1-Alcohols
- Pressure-Volume-Temperature Properties for 1-Octanol + Acetophenone, Poly(Propylene Glycol) + 1-Octanol + Acetophenone, and Poly(Ethylene Glycol) + Poly(Ethylene Glycol Methyl Ether) + Anisole
- Octanol/Water Partition Coefficient of Selected Herbicides: Determination Using Shake-Flask Method and Reversed-Phase High-Performance Liquid Chromatography
- Density and Relative Permittivity for 1-Alkanols + Dodecane at 298.15 K
- Measurement of Density and Viscosity of Binary 1-Alkanol Systems (C8-C11) at 101 kPa and Temperatures from (283.15 to 313.15) K
- Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Solubility of Berberine Chloride in Various Solvents
- Density and Surface Tension Variation with Temperature for Heptane + 1-Alkanol
- Densities, Viscosities, and Ultrasonic Velocity Studies of Binary Mixtures of Chloroform with Octan-1-ol and Decan-1-ol at (303.15 and 313.15) K
- Effect of Pressure on the Static Relative Permittivities of Alkan-1-ols at 298.15 K
- Densities, Viscosities, and Speed of Sound Studies of Binary Mixtures of Methylbenzene with Heptan-1-ol, Octan-1-ol, and Decan-1-ol at (303.15 and 313.15) K
- 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
- Thermodynamics of Mixing Tetrahydropyran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Speeds of Sound, Densities, Isobaric Thermal Expansion, Compressibilities, and Internal Pressures of Heptan-1-ol, Octan-1-ol, Nonan-1-ol, and Decan-1-ol at Temperatures from (293 to 318) K and Pressures up to 100 MPa
- Determination and Correlation for Solubilities of Ofloxacin, Norfloxacin, Lomefloxacin, Ciprofloxacin, Pefloxacin, and Pipemidic Acid in 1-Octanol from (293.15 to 333.15) K
- Density, Viscosity, and Speed of Sound of (1-Octanol + 2-Methoxyethanol), (1-Octanol + N,N-Dimethylacetamide), and (1-Octanol + Acetophenone) at Temperatures of (298.15, 308.15, and 318.15) K
- Thermodynamics of Dissolution for Bis(triazine)-Bipyridine-Class Ligands in Different Diluents and Its Reflection on Extraction
- Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
- Measurements, Correlations, and Mod. UNIFAC (Do) Prediction of (Solid-Liquid) Phase Equilibria Diagrams in Binary Systems (Aliphatic Ketone + an Alcohol)
- Liquid-Liquid Phase Behavior of Solutions of 1-Hexyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C6mimNTf2) in n-Alkyl Alcohols
- Measurement and Study on the Liquid Liquid Equilibrium of Ionic Liquids with Aliphatic Alcohols
- Densities and Viscosities of Four Binary Diethyl Carbonate + 1-Alcohol Systems from (288.15 to 313.15) K
- Micellar Properties and Related Thermodynamic Parameters of Aqueous Anionic Surfactants in the Presence of Monohydric Alcohols
- Liquid Liquid Phase Equilibria of 1-Propanol + Water + n-Alcohol Ternary Systems at 298.15 K and Atmospheric Pressure
- Liquid Liquid Phase Behavior of Solutions of 1-Butyl-3-methylimidazolium Bis((trifluoromethyl)sulfonyl)amide (C4mimNTf2) in n-Alkyl Alcohols
- Acidity and Hydrophobicity of Several New Potential Antitubercular Drugs: Isoniazid and Benzimidazole Derivatives
- Solubility of Water in Octan-1-ol from (275 to 369) K
- Octanol/Air Partition Coefficients of Volatile Methylsiloxanes and Their Temperature Dependence
- Densities and Viscosities of Three Binary Monoglyme + 1-Alcohol Systems from (283.15 to 313.15) K
- Chemical Equilibrium of the Liquid-Phase Dehydration of 1-Octanol to 1-(Octyloxy)octane
- 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
- Experimental Study of Chemical Equilibria in the Liquid-Phase Reaction between 1-Octanol and Ethanol to 1-Ethoxyoctane
- Solubility and Transfer Processes of Some Hydrazones in Biologically Relevant Solvents
- Density and Viscosity of the Binary Systems Ethanol + Butan-1-ol, + Pentan-1-ol, + Heptan-1-ol, + Octan-1-ol, Nonan-1-ol, + Decan-1-ol at 0.1 MPa and Temperatures from 283.15 K to 313.15 K
- Solubility Determination and Correlation of (2R,3S,4S,5S)-6-(Hydroxymethyl)-tetrahydro-2H-pyran-2,3,4, 5-tetraol in Fatty Alcohol
- Solubility and Solution Thermodynamics of Novel Bicyclic Derivatives of 1,3-Selenazine in Biological Relevant Solvents
- Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
- Impact of Sulfonamide Structure on Solubility and Transfer Processes in Biologically Relevant Solvents
- 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, Isothermal Compressibilities, and Isobaric Thermal Expansivities of Hexan-2-ol, Octan-1-ol, and Decan-1-ol from (313 to 363) K and Pressures up to 22 MPa
- Thermodynamics of Mixing Tetrahydrofuran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
- Liquid Phase Behavior of Ionic Liquids with Water and 1-Octanol and Modeling of 1-Octanol/Water Partition Coefficients
- Densities and Excess Molar Volumes of N-Methylmorpholine + 1-Alkanol Systems at 298.15 K
- 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
- Thermophysical Properties of an Insensitive Munitions Compound, 2,4-Dinitroanisole
- Solubilities of Benzoic Acid, p-Methylbenzoic Acid, m-Methylbenzoic Acid, o-Methylbenzoic Acid, p-Hydroxybenzoic Acid, and o-Nitrobenzoic Acid in 1-Octanol
- Solubility of 1-Alkyl-3-ethylimidazolium-Based Ionic Liquids in Water and 1-Octanol
- Solubility of Rifapentine in the Binary System of Acetic Acid and n-Octanol Solvent Mixtures
- Solubility of the Antimicrobial Agent Triclosan in Organic Solvents of Different Hydrogen Bonding Capabilities at Several Temperatures
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Solubilities of Sulfamethazine, Sulfadimethoxine, Sulfamethoxydiazine, Sulfamonomethoxine, Sulfamethoxazole, and Sulfaquinoxaline in 1-Octanol from (298.15 to 333.15) K
- Determination of Octanol-Air Partition Coefficients (KOA) of Fluorotelomer Acrylates, Perfluoroalkyl Sulfonamids, and Perfluoroalkylsulfonamido Ethanols
- Octanol/Water Partition Coefficients of Sulfonamides: Experimental Determination and Calculation Using Physicochemical Descriptors
- Temperature Effect on the Distribution of Some Phenolic Compounds: An Experimental Measurement of 1-Octanol/Water Partition Coefficients
- Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
- Interfacial Properties, Densities, and Contact Angles of Task Specific Ionic Liquids
- 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
- Solid-Liquid Equilibria, Excess Molar Volumes, and Molar Refractivity Deviations for Extractive Solvents of Molybdenum
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Liquid-Liquid Phase Behavior of Solutions of 1-Octyl- and 1-Decyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide (C8,10mimNTf2) in n-Alkyl Alcohols
- Density and Viscosity of Binary Mixtures of {1-Butyl-3-methylimidazolium Thiocyanate + 1-Heptanol, 1-Octanol, 1-Nonanol, or 1-Decanol}
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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