- InChI
- InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3
- InChI Key
- YNQLUTRBYVCPMQ-UHFFFAOYSA-N
- Formula
- C8H10
- SMILES
- CCc1ccccc1
- Molecular Weight1
- 106.17
- CAS
- 100-41-4
- Other Names
-
- .alpha.-methyltoluene
- Aethylbenzol
- EB
- Ethylbenzeen
- Ethylbenzol
- Etilbenzene
- Etylobenzen
- NCI-C56393
- NSC 406903
- UN 1175
- ethylbenzene
- phenylethane
- «alpha»-Methyltoluene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Csat : Molar heat capacity at saturation pressure (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- 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.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3020; 0.3040] |
|
|
| ω | 0.3040 | ChemSep v8.3 pure component data | |
| ω | 0.3020 | KDB | |
| PAff | [788.00; 789.90] | kJ/mol |
|
| PAff | 788.00 | kJ/mol | NIST |
| PAff | 789.90 | kJ/mol | NIST |
| Tig | [705.15; 733.15] | K |
|
| Tig | 733.15 | K | KDB |
| Tig | 705.15 | K | NCMS SOLV-DB |
| BasG | [760.20; 760.30] | kJ/mol |
|
| BasG | 760.30 | kJ/mol | NIST |
| BasG | 760.20 | kJ/mol | NIST |
| ΔcH°liquid | [-4584.00; -4557.60] | kJ/mol |
|
| ΔcH°liquid | -4562.40 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -4564.87 ± 0.71 | kJ/mol | NIST |
| ΔcH°liquid | -4566.40 | kJ/mol | NIST |
| ΔcH°liquid | -4557.60 | kJ/mol | NIST |
| ΔcH°liquid | -4565.90 | kJ/mol | NIST |
| ΔcH°liquid | Outlier -4584.00 | kJ/mol | NIST |
| Cp,liquid | 185.44 | J/mol×K | Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile) |
| μ | [0.40; 0.60] | debye |
|
| μ | 0.60 | debye | ChemSep v8.3 pure component data |
| μ | 0.40 | debye | KDB |
| εr | 2.04 | NCMS SOLV-DB | |
| LFL | 1.00 | % in Air | KDB |
| UFL | 6.70 | % in Air | KDB |
| Tflash,cc | [291.15; 299.82] | K |
|
| Tflash,cc | 299.82 | K | KDB |
| Tflash,cc | 291.15 | K | NCMS SOLV-DB |
| Tflash,oc | 288.15 | K | KDB |
| ΔfG° | [130.70; 130.73] | kJ/mol |
|
| ΔfG° | 130.73 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | 130.70 | kJ/mol | KDB |
| Rg | 3.8210 | KDB | |
| Δc,grossH | 4564.87 | kJ/mol | KDB |
| Δc,netH | 4344.792 | kJ/mol | KDB |
| ΔfH°gas | [29.80; 69.30] | kJ/mol |
|
| ΔfH°gas | 29.92 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | 29.81 | kJ/mol | KDB |
| ΔfH°gas | 29.80 ± 0.84 | kJ/mol | NIST |
| ΔfH°gas | 49.00 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | 69.30 | kJ/mol | NIST |
| ΔfH°liquid | [-12.50; 27.00] | kJ/mol |
|
| ΔfH°liquid | -12.50 ± 0.84 | kJ/mol | NIST |
| ΔfH°liquid | 6.80 ± 4.00 | kJ/mol | NIST |
| ΔfH°liquid | 27.00 | kJ/mol | NIST |
| ΔfusH° | 10.52 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [36.00; 42.40] | kJ/mol |
|
| ΔvapH° | 42.25 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 42.26 | kJ/mol | NIST |
| ΔvapH° | 42.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.30 | kJ/mol | NIST |
| ΔvapH° | 42.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 42.24 | kJ/mol | NIST |
| ΔvapH° | 42.30 | kJ/mol | NIST |
| ΔvapH° | Outlier 36.00 ± 0.20 | kJ/mol | NIST |
| IE | [8.61; 9.38] | eV |
|
| IE | 8.77 ± 0.01 | eV | NIST |
| IE | 8.77 | eV | NIST |
| IE | 8.61 | eV | NIST |
| IE | 8.65 ± 0.10 | eV | NIST |
| IE | 8.76 | eV | NIST |
| IE | 8.77 ± 0.01 | eV | NIST |
| IE | 8.75 ± 0.05 | eV | NIST |
| IE | 8.76 ± 0.01 | eV | NIST |
| IE | 8.77 ± 0.01 | eV | NIST |
| IE | 8.77 | eV | NIST |
| IE | 8.73 | eV | NIST |
| IE | Outlier 9.38 | eV | NIST |
| log10WS | [-2.77; -2.77] |
|
|
| log10WS | -2.77 | Aq. Solubility Prediction | |
| log10WS | -2.77 | Estimated Solubility | |
| logPoct/wat | 3.150 | NCMS SOLV-DB | |
| McVol | 99.820 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=3); %!d(float64=3)] |
|
|
| NFPA Fire | 3 | KDB | |
| NFPA Fire | 3 | NCMS SOLV-DB | |
| NFPA Health | [%!d(float64=2); %!d(float64=2)] |
|
|
| NFPA Health | 2 | KDB | |
| NFPA Health | 2 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [3608.80; 3740.00] | kPa |
|
| Pc | 3609.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 3609.00 | kPa | KDB |
| Pc | 3609.00 ± 10.00 | kPa | NIST |
| Pc | 3608.80 ± 5.00 | kPa | NIST |
| Pc | 3649.00 ± 6.89 | kPa | NIST |
| Pc | 3619.00 ± 41.37 | kPa | NIST |
| Pc | 3609.00 ± 0.10 | kPa | NIST |
| Pc | Outlier 3740.00 ± 7.84 | kPa | NIST |
| Ptriple | 3.91e-06 | kPa | ChemSep v8.3 pure component data |
| ρc | [283.46; 284.52] | kg/m3 |
|
| ρc | 284.52 ± 1.06 | kg/m3 | NIST |
| ρc | 283.46 ± 4.25 | kg/m3 | NIST |
| Inp | [118.30; 893.00] |
|
|
| Inp | 850.60 | NIST | |
| Inp | 844.50 | NIST | |
| Inp | 846.80 | NIST | |
| Inp | 843.40 | NIST | |
| Inp | 841.80 | NIST | |
| Inp | 843.50 | NIST | |
| Inp | 848.10 | NIST | |
| Inp | 866.85 | NIST | |
| Inp | 879.95 | NIST | |
| Inp | 847.30 | NIST | |
| Inp | 875.40 | NIST | |
| Inp | 848.34 | NIST | |
| Inp | 848.34 | NIST | |
| Inp | 859.20 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 854.80 | NIST | |
| Inp | 871.10 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 847.80 | NIST | |
| Inp | 848.10 | NIST | |
| Inp | 848.10 | NIST | |
| Inp | 848.20 | NIST | |
| Inp | 847.60 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 858.40 | NIST | |
| Inp | 863.30 | NIST | |
| Inp | 857.30 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 849.70 | NIST | |
| Inp | 834.60 | NIST | |
| Inp | 839.80 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 832.80 | NIST | |
| Inp | 838.50 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 833.30 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 847.80 | NIST | |
| Inp | 848.20 | NIST | |
| Inp | 851.40 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 845.30 | NIST | |
| Inp | 847.70 | NIST | |
| Inp | 858.90 | NIST | |
| Inp | 864.20 | NIST | |
| Inp | 870.10 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 834.10 | NIST | |
| Inp | 839.50 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 844.80 | NIST | |
| Inp | 845.30 | NIST | |
| Inp | 839.40 | NIST | |
| Inp | 840.60 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 839.20 | NIST | |
| Inp | 845.30 | NIST | |
| Inp | 847.70 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 855.20 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 841.56 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 847.70 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 844.20 | NIST | |
| Inp | 851.30 | NIST | |
| Inp | 844.30 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 864.10 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 855.60 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 850.80 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 856.30 | NIST | |
| Inp | 855.50 | NIST | |
| Inp | 853.20 | NIST | |
| Inp | 856.30 | NIST | |
| Inp | 857.20 | NIST | |
| Inp | 839.80 | NIST | |
| Inp | 868.30 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 834.00 | NIST | |
| Inp | 860.90 | NIST | |
| Inp | 836.10 | NIST | |
| Inp | 841.70 | NIST | |
| Inp | 846.10 | NIST | |
| Inp | 846.40 | NIST | |
| Inp | 861.50 | NIST | |
| Inp | 853.20 | NIST | |
| Inp | 856.30 | NIST | |
| Inp | 857.20 | NIST | |
| Inp | 856.30 | NIST | |
| Inp | 855.50 | NIST | |
| Inp | 844.19 | NIST | |
| Inp | 844.47 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 844.50 | NIST | |
| Inp | 844.74 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 848.30 | NIST | |
| Inp | 856.20 | NIST | |
| Inp | 848.30 | NIST | |
| Inp | 848.30 | NIST | |
| Inp | 856.20 | NIST | |
| Inp | 845.17 | NIST | |
| Inp | 845.49 | NIST | |
| Inp | 848.70 | NIST | |
| Inp | 844.80 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 841.26 | NIST | |
| Inp | 844.05 | NIST | |
| Inp | 845.90 | NIST | |
| Inp | 857.33 | NIST | |
| Inp | 860.40 | NIST | |
| Inp | 862.45 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 870.79 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 831.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 836.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 863.30 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 847.66 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 868.10 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 856.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 835.30 | NIST | |
| Inp | 837.60 | NIST | |
| Inp | 840.80 | NIST | |
| Inp | 843.30 | NIST | |
| Inp | 845.30 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 835.00 | NIST | |
| Inp | 837.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 857.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 839.30 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 853.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 851.00 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 861.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 859.10 | NIST | |
| Inp | 863.30 | NIST | |
| Inp | 862.80 | NIST | |
| Inp | 862.60 | NIST | |
| Inp | 847.50 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 830.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 849.00 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 843.00 | NIST | |
| Inp | Outlier 118.80 | NIST | |
| Inp | Outlier 118.30 | NIST | |
| Inp | Outlier 134.54 | NIST | |
| Inp | Outlier 118.90 | NIST | |
| Inp | Outlier 129.41 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 840.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 859.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 846.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 847.00 | NIST | |
| Inp | 862.80 | NIST | |
| Inp | 858.00 | NIST | |
| Inp | 845.00 | NIST | |
| Inp | 852.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 847.66 | NIST | |
| Inp | 842.00 | NIST | |
| Inp | 848.00 | NIST | |
| Inp | 843.30 | NIST | |
| Inp | 841.00 | NIST | |
| Inp | Outlier 118.80 | NIST | |
| Inp | 850.60 | NIST | |
| Inp | 843.50 | NIST | |
| Inp | 875.40 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 847.60 | NIST | |
| Inp | 863.30 | NIST | |
| Inp | 834.60 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 870.10 | NIST | |
| Inp | 844.60 | NIST | |
| Inp | 839.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 841.56 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 849.10 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 851.30 | NIST | |
| I | [1098.00; 1180.00] |
|
|
| I | 1125.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1105.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1131.90 | NIST | |
| I | 1158.90 | NIST | |
| I | 1164.30 | NIST | |
| I | Outlier 1169.80 | NIST | |
| I | Outlier 1175.20 | NIST | |
| I | 1136.00 | NIST | |
| I | 1160.90 | NIST | |
| I | 1158.40 | NIST | |
| I | 1159.40 | NIST | |
| I | 1127.10 | NIST | |
| I | 1111.10 | NIST | |
| I | Outlier 1178.00 | NIST | |
| I | 1154.00 | NIST | |
| I | 1162.00 | NIST | |
| I | Outlier 1169.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1098.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1146.10 | NIST | |
| I | 1123.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1115.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1133.00 | NIST | |
| I | Outlier 1168.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1128.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1107.00 | NIST | |
| I | 1133.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1157.00 | NIST | |
| I | Outlier 1168.00 | NIST | |
| I | Outlier 1180.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1145.00 | NIST | |
| I | 1144.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1157.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1146.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1142.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1104.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1114.00 | NIST | |
| I | 1118.00 | NIST | |
| I | 1141.00 | NIST | |
| I | 1108.00 | NIST | |
| I | 1147.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1135.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1126.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1124.00 | NIST | |
| I | 1134.00 | NIST | |
| I | 1139.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1122.00 | NIST | |
| I | 1119.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1130.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1121.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1127.00 | NIST | |
| I | 1125.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1109.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1111.00 | NIST | |
| I | 1131.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1132.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1110.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1120.00 | NIST | |
| I | 1100.00 | NIST | |
| I | 1164.30 | NIST | |
| I | 1158.40 | NIST | |
| I | 1154.00 | NIST | |
| I | 1116.00 | NIST | |
| I | 1129.00 | NIST | |
| I | 1115.00 | NIST | |
| I | Outlier 1168.00 | NIST | |
| I | 1138.00 | NIST | |
| I | 1123.00 | NIST | |
| I | 1135.00 | NIST | |
| S°gas | 360.60 ± 0.50 | J/mol×K | NIST |
| S°liquid | [255.01; 256.10] | J/mol×K |
|
| S°liquid | 255.01 | J/mol×K | NIST |
| S°liquid | 256.10 | J/mol×K | NIST |
| Tboil | [136.00; 429.60] | K |
|
| Tboil | 409.35 | K | Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa |
| Tboil | 409.35 | K | Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa |
| Tboil | 409.32 | K | Isobaric Vapor-Liquid Equilibium for the Binary Systems of Methyl Formate with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.33 kPa |
| Tboil | 409.25 | K | Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide |
| Tboil | 409.36 | K | ChemSep v8.3 pure component data |
| Tboil | 409.34 | K | KDB |
| Tboil | 409.34 | K | NCMS SOLV-DB |
| Tboil | 409.15 ± 0.20 | K | NIST |
| Tboil | 409.40 | K | NIST |
| Tboil | 409.35 ± 0.13 | K | NIST |
| Tboil | 409.35 ± 0.30 | K | NIST |
| Tboil | 409.35 ± 0.10 | K | NIST |
| Tboil | 409.35 ± 0.10 | K | NIST |
| Tboil | 409.30 | K | NIST |
| Tboil | 409.35 ± 0.30 | K | NIST |
| Tboil | 409.00 ± 0.30 | K | NIST |
| Tboil | 409.33 ± 0.20 | K | NIST |
| Tboil | 409.35 | K | NIST |
| Tboil | 409.33 ± 0.20 | K | NIST |
| Tboil | 409.35 ± 0.20 | K | NIST |
| Tboil | 409.30 ± 0.20 | K | NIST |
| Tboil | 409.25 ± 0.30 | K | NIST |
| Tboil | 409.30 ± 0.20 | K | NIST |
| Tboil | 409.40 ± 0.60 | K | NIST |
| Tboil | 409.45 ± 0.30 | K | NIST |
| Tboil | 409.34 ± 0.30 | K | NIST |
| Tboil | 409.50 ± 0.30 | K | NIST |
| Tboil | 411.90 ± 2.00 | K | NIST |
| Tboil | 409.35 ± 0.30 | K | NIST |
| Tboil | 409.35 ± 0.25 | K | NIST |
| Tboil | 409.35 ± 0.30 | K | NIST |
| Tboil | 409.33 ± 0.30 | K | NIST |
| Tboil | 409.45 ± 0.40 | K | NIST |
| Tboil | 408.15 ± 2.00 | K | NIST |
| Tboil | 409.33 ± 0.25 | K | NIST |
| Tboil | 408.15 ± 1.50 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tboil | 409.20 ± 0.50 | K | NIST |
| Tboil | Outlier 136.10 ± 0.30 | K | NIST |
| Tboil | Outlier 136.40 ± 0.40 | K | NIST |
| Tboil | 407.00 ± 3.00 | K | NIST |
| Tboil | 409.40 ± 0.50 | K | NIST |
| Tboil | 408.15 ± 2.00 | K | NIST |
| Tboil | 409.50 ± 0.50 | K | NIST |
| Tboil | 409.33 ± 0.02 | K | NIST |
| Tboil | 410.00 ± 2.00 | K | NIST |
| Tboil | 409.15 ± 1.00 | K | NIST |
| Tboil | 409.00 ± 2.00 | K | NIST |
| Tboil | 409.40 ± 0.50 | K | NIST |
| Tboil | 409.35 ± 0.50 | K | NIST |
| Tboil | 409.33 ± 0.10 | K | NIST |
| Tboil | 408.70 ± 0.40 | K | NIST |
| Tboil | 409.40 ± 0.15 | K | NIST |
| Tboil | 409.30 ± 0.40 | K | NIST |
| Tboil | 409.30 ± 0.30 | K | NIST |
| Tboil | 409.33 ± 0.01 | K | NIST |
| Tboil | 409.40 ± 0.20 | K | NIST |
| Tboil | 409.45 ± 0.50 | K | NIST |
| Tboil | 409.70 ± 0.30 | K | NIST |
| Tboil | 409.34 ± 0.06 | K | NIST |
| Tboil | 409.10 ± 0.30 | K | NIST |
| Tboil | 409.55 ± 0.30 | K | NIST |
| Tboil | 409.30 ± 0.20 | K | NIST |
| Tboil | 409.15 ± 1.00 | K | NIST |
| Tboil | 429.60 | K | NIST |
| Tboil | 409.65 ± 0.30 | K | NIST |
| Tboil | 409.47 ± 0.10 | K | NIST |
| Tboil | 409.30 ± 0.30 | K | NIST |
| Tboil | 409.00 ± 4.00 | K | NIST |
| Tboil | 408.15 ± 1.50 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 409.25 ± 0.70 | K | NIST |
| Tboil | 409.30 ± 0.10 | K | NIST |
| Tboil | 408.15 ± 1.50 | K | NIST |
| Tboil | 409.25 ± 0.50 | K | NIST |
| Tboil | 409.15 ± 1.50 | K | NIST |
| Tboil | 408.95 ± 1.00 | K | NIST |
| Tboil | 409.20 ± 0.15 | K | NIST |
| Tboil | 409.15 ± 1.00 | K | NIST |
| Tboil | 409.55 ± 0.70 | K | NIST |
| Tboil | 409.30 ± 0.30 | K | NIST |
| Tboil | 409.30 ± 0.50 | K | NIST |
| Tboil | 409.30 ± 0.50 | K | NIST |
| Tboil | 409.25 ± 0.30 | K | NIST |
| Tboil | 409.30 ± 0.25 | K | NIST |
| Tboil | 408.65 ± 2.00 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 409.00 ± 2.00 | K | NIST |
| Tboil | Outlier 136.00 ± 0.50 | K | NIST |
| Tboil | 409.20 ± 0.25 | K | NIST |
| Tboil | 408.00 ± 4.00 | K | NIST |
| Tboil | 408.70 ± 1.50 | K | NIST |
| Tboil | 409.50 ± 0.30 | K | NIST |
| Tboil | 409.00 ± 2.00 | K | NIST |
| Tboil | 407.65 ± 2.00 | K | NIST |
| Tboil | 409.15 ± 2.00 | K | NIST |
| Tboil | 409.30 ± 0.20 | K | NIST |
| Tboil | 409.00 ± 2.00 | K | NIST |
| Tboil | 408.80 ± 0.50 | K | NIST |
| Tboil | 412.45 ± 0.50 | K | NIST |
| Tboil | 407.00 ± 2.00 | K | NIST |
| Tboil | 409.10 ± 1.50 | K | NIST |
| Tc | [616.80; 619.60] | K |
|
| Tc | 617.15 | K | ChemSep v8.3 pure component data |
| Tc | 617.15 | K | KDB |
| Tc | 617.20 ± 0.10 | K | NIST |
| Tc | 617.20 ± 0.10 | K | NIST |
| Tc | 617.10 | K | NIST |
| Tc | 616.80 ± 0.50 | K | NIST |
| Tc | 618.20 ± 0.70 | K | NIST |
| Tc | 616.80 ± 0.50 | K | NIST |
| Tc | 617.07 ± 0.10 | K | NIST |
| Tc | 617.12 ± 0.20 | K | NIST |
| Tc | 617.20 ± 0.40 | K | NIST |
| Tc | Outlier 619.60 ± 2.00 | K | NIST |
| Tfus | [171.90; 278.29] | K |
|
| Tfus | Outlier 278.29 | K | Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water) |
| Tfus | 178.20 | K | ChemSep v8.3 pure component data |
| Tfus | 178.20 | K | KDB |
| Tfus | 178.20 | K | Aq. Solubility Prediction |
| Tfus | 178.17 | K | NCMS SOLV-DB |
| Tfus | 178.15 ± 0.20 | K | NIST |
| Tfus | 178.15 ± 0.20 | K | NIST |
| Tfus | 178.15 | K | NIST |
| Tfus | 178.20 ± 2.00 | K | NIST |
| Tfus | 179.50 ± 0.60 | K | NIST |
| Tfus | 178.06 ± 0.01 | K | NIST |
| Tfus | 178.14 ± 0.15 | K | NIST |
| Tfus | 178.17 ± 0.03 | K | NIST |
| Tfus | 178.37 ± 0.06 | K | NIST |
| Tfus | 171.90 ± 0.50 | K | NIST |
| Tfus | 181.15 ± 2.00 | K | NIST |
| Tfus | 178.10 ± 0.60 | K | NIST |
| Tfus | 177.89 ± 0.15 | K | NIST |
| Tfus | 178.80 ± 0.50 | K | NIST |
| Tfus | 180.80 ± 1.00 | K | NIST |
| Tfus | 179.25 ± 0.40 | K | NIST |
| Tfus | 179.00 ± 1.00 | K | NIST |
| Ttriple | [178.00; 178.20] | K |
|
| Ttriple | 178.20 | K | ChemSep v8.3 pure component data |
| Ttriple | 178.15 ± 0.02 | K | NIST |
| Ttriple | 178.00 ± 0.30 | K | NIST |
| Ttriple | 178.15 ± 0.02 | K | NIST |
| Ttriple | 178.00 ± 0.30 | K | NIST |
| UQi | 3.51 | ChemSep v8.3 pure component data | |
| URi | 4.60 | ChemSep v8.3 pure component data | |
| Vc | [0.374; 0.374] | m3/kmol |
|
| Vc | 0.374 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.374 | m3/kmol | KDB |
| Vc | 0.374 | m3/kmol | NIST |
| Zc | [0.2630000; 0.2630460] |
|
|
| Zc | 0.2630000 | ChemSep v8.3 pure component data | |
| Zc | 0.2630460 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 408.75 | K | 95.30 | Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 253.23 | 100.00 | 0.0012 |
| 253.22 | 1000.00 | 0.0012 |
| 253.21 | 5000.00 | 0.0013 |
| 253.22 | 10000.00 | 0.0013 |
| 253.24 | 15000.00 | 0.0014 |
| 253.23 | 20000.00 | 0.0014 |
| 253.23 | 25000.00 | 0.0015 |
| 253.24 | 30000.00 | 0.0015 |
| 253.22 | 35000.00 | 0.0016 |
| 263.22 | 100.00 | 0.0010 |
| 263.22 | 1000.00 | 0.0010 |
| 263.21 | 5000.00 | 0.0011 |
| 263.20 | 10000.00 | 0.0011 |
| 263.20 | 15000.00 | 0.0012 |
| 263.21 | 20000.00 | 0.0012 |
| 263.21 | 25000.00 | 0.0013 |
| 263.22 | 30000.00 | 0.0013 |
| 263.21 | 35000.00 | 0.0014 |
| 273.21 | 100.00 | 0.0009 |
| 273.17 | 1000.00 | 0.0009 |
| 273.15 | 5000.00 | 0.0009 |
| 273.18 | 10000.00 | 0.0010 |
| 273.19 | 15000.00 | 0.0010 |
| 273.15 | 20000.00 | 0.0010 |
| 273.16 | 25000.00 | 0.0011 |
| 273.15 | 30000.00 | 0.0011 |
| 273.15 | 35000.00 | 0.0012 |
| 283.16 | 100.00 | 0.0008 |
| 283.13 | 1000.00 | 0.0008 |
| 283.16 | 5000.00 | 0.0008 |
| 283.14 | 10000.00 | 0.0008 |
| 283.17 | 15000.00 | 0.0009 |
| 283.15 | 20000.00 | 0.0009 |
| 283.17 | 25000.00 | 0.0009 |
| 283.16 | 30000.00 | 0.0010 |
| 283.16 | 35000.00 | 0.0010 |
| 293.26 | 100.00 | 0.0007 |
| 293.20 | 1000.00 | 0.0007 |
| 293.18 | 5000.00 | 0.0007 |
| 293.24 | 10000.00 | 0.0007 |
| 293.23 | 15000.00 | 0.0008 |
| 293.24 | 20000.00 | 0.0008 |
| 293.22 | 25000.00 | 0.0008 |
| 293.24 | 30000.00 | 0.0008 |
| 293.26 | 35000.00 | 0.0009 |
| 303.15 | 100.00 | 0.0006 |
| 303.17 | 1000.00 | 0.0006 |
| 303.18 | 5000.00 | 0.0006 |
| 303.20 | 10000.00 | 0.0006 |
| 303.19 | 15000.00 | 0.0007 |
| 303.17 | 20000.00 | 0.0007 |
| 303.18 | 25000.00 | 0.0007 |
| 303.19 | 30000.00 | 0.0008 |
| 303.18 | 35000.00 | 0.0008 |
| 313.12 | 100.00 | 0.0005 |
| 313.12 | 1000.00 | 0.0005 |
| 313.11 | 5000.00 | 0.0006 |
| 313.10 | 10000.00 | 0.0006 |
| 313.12 | 15000.00 | 0.0006 |
| 313.09 | 20000.00 | 0.0006 |
| 313.10 | 25000.00 | 0.0006 |
| 313.08 | 30000.00 | 0.0007 |
| 313.10 | 35000.00 | 0.0007 |
| 322.97 | 100.00 | 0.0005 |
| 322.98 | 1000.00 | 0.0005 |
| 322.98 | 5000.00 | 0.0005 |
| 322.98 | 10000.00 | 0.0005 |
| 322.98 | 15000.00 | 0.0005 |
| 322.97 | 20000.00 | 0.0006 |
| 322.98 | 25000.00 | 0.0006 |
| 322.98 | 30000.00 | 0.0006 |
| 322.98 | 35000.00 | 0.0006 |
| 332.91 | 100.00 | 0.0004 |
| 332.92 | 1000.00 | 0.0004 |
| 332.91 | 5000.00 | 0.0005 |
| 332.92 | 10000.00 | 0.0005 |
| 332.92 | 15000.00 | 0.0005 |
| 332.92 | 20000.00 | 0.0005 |
| 332.92 | 25000.00 | 0.0005 |
| 332.92 | 30000.00 | 0.0006 |
| 332.92 | 35000.00 | 0.0006 |
| 342.81 | 100.00 | 0.0004 |
| 342.80 | 1000.00 | 0.0004 |
| 342.81 | 5000.00 | 0.0004 |
| 342.80 | 10000.00 | 0.0004 |
| 342.80 | 15000.00 | 0.0005 |
| 342.80 | 20000.00 | 0.0005 |
| 342.80 | 25000.00 | 0.0005 |
| 342.80 | 30000.00 | 0.0005 |
| 342.80 | 35000.00 | 0.0005 |
| 352.73 | 100.00 | 0.0004 |
| 352.73 | 1000.00 | 0.0004 |
| 352.72 | 5000.00 | 0.0004 |
| 352.73 | 10000.00 | 0.0004 |
| 352.73 | 15000.00 | 0.0004 |
| 352.72 | 20000.00 | 0.0004 |
| 352.73 | 25000.00 | 0.0004 |
| 352.73 | 30000.00 | 0.0005 |
| 352.72 | 35000.00 | 0.0005 |
| 362.66 | 100.00 | 0.0003 |
| 362.66 | 1000.00 | 0.0003 |
| 362.66 | 5000.00 | 0.0004 |
| 362.67 | 10000.00 | 0.0004 |
| 362.66 | 15000.00 | 0.0004 |
| 362.66 | 20000.00 | 0.0004 |
| 362.66 | 25000.00 | 0.0004 |
| 362.66 | 30000.00 | 0.0004 |
| 362.67 | 35000.00 | 0.0004 |
| 372.61 | 100.00 | 0.0003 |
| 372.60 | 1000.00 | 0.0003 |
| 372.59 | 5000.00 | 0.0003 |
| 372.59 | 10000.00 | 0.0003 |
| 372.59 | 15000.00 | 0.0004 |
| 372.59 | 20000.00 | 0.0004 |
| 372.59 | 25000.00 | 0.0004 |
| 372.59 | 30000.00 | 0.0004 |
| 372.59 | 35000.00 | 0.0004 |
| Reference | ||
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 93.00 | 298.15 | 1.493 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 292.25 | 100.00 | 867.0 |
| 292.25 | 5000.00 | 870.8 |
| 292.25 | 9900.00 | 874.0 |
| 292.25 | 19700.00 | 881.3 |
| 292.25 | 29500.00 | 887.1 |
| 292.25 | 39300.00 | 893.0 |
| 292.25 | 49100.00 | 898.5 |
| 292.25 | 58900.00 | 903.8 |
| 313.45 | 100.00 | 849.1 |
| 313.45 | 5000.00 | 853.1 |
| 313.45 | 19700.00 | 864.4 |
| 313.45 | 29500.00 | 871.4 |
| 313.45 | 39300.00 | 877.6 |
| 313.45 | 49100.00 | 883.6 |
| 313.45 | 58900.00 | 889.4 |
| 336.55 | 100.00 | 828.7 |
| 336.55 | 5000.00 | 833.6 |
| 336.55 | 9900.00 | 838.5 |
| 336.55 | 19700.00 | 845.8 |
| 336.55 | 29500.00 | 854.0 |
| 336.55 | 39300.00 | 860.9 |
| 336.55 | 49100.00 | 867.8 |
| 336.55 | 58900.00 | 873.6 |
| 358.81 | 100.00 | 808.4 |
| 358.81 | 5000.00 | 814.5 |
| 358.81 | 9900.00 | 820.0 |
| 358.81 | 19700.00 | 827.6 |
| 358.81 | 29500.00 | 836.8 |
| 358.81 | 39300.00 | 844.8 |
| 358.81 | 49100.00 | 852.4 |
| 358.81 | 58900.00 | 858.6 |
| 382.95 | 5000.00 | 793.0 |
| 382.95 | 9900.00 | 799.0 |
| 382.95 | 19700.00 | 808.1 |
| 382.95 | 29500.00 | 818.2 |
| 382.95 | 39300.00 | 827.1 |
| 382.95 | 49100.00 | 835.1 |
| 382.95 | 58900.00 | 842.5 |
| 408.05 | 5000.00 | 770.4 |
| 408.05 | 9900.00 | 777.3 |
| 408.05 | 19700.00 | 788.5 |
| 408.05 | 29500.00 | 799.7 |
| 408.05 | 39300.00 | 809.5 |
| 408.05 | 49100.00 | 817.9 |
| 408.05 | 58900.00 | 826.0 |
| 434.45 | 5000.00 | 746.0 |
| 434.45 | 9900.00 | 754.4 |
| 434.45 | 19700.00 | 768.1 |
| 434.45 | 29500.00 | 780.5 |
| 434.45 | 39300.00 | 791.0 |
| 434.45 | 49100.00 | 800.4 |
| 434.45 | 58900.00 | 808.6 |
| 461.85 | 5000.00 | 718.6 |
| 461.85 | 9900.00 | 728.8 |
| 461.85 | 19700.00 | 746.2 |
| 461.85 | 29500.00 | 760.0 |
| 461.85 | 39300.00 | 771.7 |
| 461.85 | 49100.00 | 782.3 |
| 461.85 | 58900.00 | 791.0 |
| 490.15 | 5000.00 | 687.0 |
| 490.15 | 9900.00 | 700.0 |
| 490.15 | 19700.00 | 720.9 |
| 490.15 | 29500.00 | 737.2 |
| 490.15 | 39300.00 | 750.7 |
| 490.15 | 49100.00 | 762.9 |
| 490.15 | 58900.00 | 773.2 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [88.32; 362.10] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 6.54340e+01 | |||
| Coefficient B | -6.19340e+02 | |||
| Coefficient C | 6.25824e+00 | |||
| Coefficient D | -1.64120e-04 | |||
| Coefficient E | 4.15290e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 88.32 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 147.58 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 202.59 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 245.45 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 278.04 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 303.05 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 322.62 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 338.31 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 351.21 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 362.10 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [156.17; 226.93] | J/mol×K | [178.17; 409.35] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.31820e+02 | |||
| Coefficient B | -9.09830e+01 | |||
| Coefficient C | 3.12324e+00 | |||
| Coefficient D | 2.65040e-03 | |||
| Coefficient E | 3.39650e-06 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 178.17 | |||
| Temperature range, max. | 409.35 | |||
| Cp,liquid | 156.17 | J/mol×K | 178.17 | Calculated Property |
| Cp,liquid | 160.56 | J/mol×K | 203.86 | Calculated Property |
| Cp,liquid | 165.41 | J/mol×K | 229.54 | Calculated Property |
| Cp,liquid | 170.86 | J/mol×K | 255.23 | Calculated Property |
| Cp,liquid | 177.06 | J/mol×K | 280.92 | Calculated Property |
| Cp,liquid | 184.19 | J/mol×K | 306.60 | Calculated Property |
| Cp,liquid | 192.47 | J/mol×K | 332.29 | Calculated Property |
| Cp,liquid | 202.14 | J/mol×K | 357.98 | Calculated Property |
| Cp,liquid | 213.51 | J/mol×K | 383.66 | Calculated Property |
| Cp,liquid | 226.93 | J/mol×K | 409.35 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0080145; 0.0001073] | Pa×s | [178.20; 617.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.45060e+01 | |||
| Coefficient B | 1.23720e+03 | |||
| Coefficient C | 5.28590e-01 | |||
| Coefficient D | -9.13630e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 617.15 | |||
| η | 0.0080145 | Pa×s | 178.20 | Calculated Property |
| η | 0.0020451 | Pa×s | 226.97 | Calculated Property |
| η | 0.0008624 | Pa×s | 275.74 | Calculated Property |
| η | 0.0004776 | Pa×s | 324.52 | Calculated Property |
| η | 0.0003116 | Pa×s | 373.29 | Calculated Property |
| η | 0.0002259 | Pa×s | 422.06 | Calculated Property |
| η | 0.0001759 | Pa×s | 470.83 | Calculated Property |
| η | 0.0001442 | Pa×s | 519.61 | Calculated Property |
| η | 0.0001227 | Pa×s | 568.38 | Calculated Property |
| η | 0.0001073 | Pa×s | 617.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [49.82; 14.94] | kJ/mol | [178.15; 594.05] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.99073e+01 | |||
| Coefficient B | 3.80483e-01 | |||
| Coefficient C | 1.09430e+00 | |||
| Coefficient D | -2.18554e+00 | |||
| Coefficient E | 1.13690e+00 | |||
| Critical temperature, Tc (K) | 6.17150e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 178.15 | |||
| Temperature range, max. | 594.05 | |||
| ΔvapH | 49.82 | kJ/mol | 178.15 | Calculated Property |
| ΔvapH | 46.85 | kJ/mol | 224.36 | Calculated Property |
| ΔvapH | 43.97 | kJ/mol | 270.57 | Calculated Property |
| ΔvapH | 41.19 | kJ/mol | 316.78 | Calculated Property |
| ΔvapH | 38.47 | kJ/mol | 362.99 | Calculated Property |
| ΔvapH | 35.67 | kJ/mol | 409.21 | Calculated Property |
| ΔvapH | 32.58 | kJ/mol | 455.42 | Calculated Property |
| ΔvapH | 28.83 | kJ/mol | 501.63 | Calculated Property |
| ΔvapH | 23.66 | kJ/mol | 547.84 | Calculated Property |
| ΔvapH | 14.94 | kJ/mol | 594.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [297.90; 436.98] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44625e+01 | |||
| Coefficient B | -3.59099e+03 | |||
| Coefficient C | -4.45680e+01 | |||
| Temperature range, min. | 297.90 | |||
| Temperature range, max. | 436.98 | |||
| Pvap | 1.33 | kPa | 297.90 | Calculated Property |
| Pvap | 3.01 | kPa | 313.35 | Calculated Property |
| Pvap | 6.23 | kPa | 328.81 | Calculated Property |
| Pvap | 11.94 | kPa | 344.26 | Calculated Property |
| Pvap | 21.50 | kPa | 359.71 | Calculated Property |
| Pvap | 36.62 | kPa | 375.17 | Calculated Property |
| Pvap | 59.47 | kPa | 390.62 | Calculated Property |
| Pvap | 92.68 | kPa | 406.07 | Calculated Property |
| Pvap | 139.26 | kPa | 421.53 | Calculated Property |
| Pvap | 202.65 | kPa | 436.98 | Calculated Property |
| Pvap | [1.27e-06; 3809.13] | kPa | [178.20; 617.20] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30601e+02 | |||
| Coefficient B | -9.74507e+03 | |||
| Coefficient C | -1.73446e+01 | |||
| Coefficient D | 1.27987e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 617.20 | |||
| Pvap | 1.27e-06 | kPa | 178.20 | Calculated Property |
| Pvap | 3.13e-03 | kPa | 226.98 | Calculated Property |
| Pvap | 0.29 | kPa | 275.76 | Calculated Property |
| Pvap | 5.09 | kPa | 324.53 | Calculated Property |
| Pvap | 35.11 | kPa | 373.31 | Calculated Property |
| Pvap | 140.03 | kPa | 422.09 | Calculated Property |
| Pvap | 401.11 | kPa | 470.87 | Calculated Property |
| Pvap | 939.77 | kPa | 519.64 | Calculated Property |
| Pvap | 1954.77 | kPa | 568.42 | Calculated Property |
| Pvap | 3809.13 | kPa | 617.20 | Calculated Property |
| Pvap | [4.05e-06; 3587.82] | kPa | [178.15; 617.17] |
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 | 7.97937e+01 | |||
| Coefficient B | -7.63808e+03 | |||
| Coefficient C | -9.55398e+00 | |||
| Coefficient D | 5.65318e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 178.15 | |||
| Temperature range, max. | 617.17 | |||
| Pvap | 4.05e-06 | kPa | 178.15 | Calculated Property |
| Pvap | 4.51e-03 | kPa | 226.93 | Calculated Property |
| Pvap | 0.31 | kPa | 275.71 | Calculated Property |
| Pvap | 4.99 | kPa | 324.49 | Calculated Property |
| Pvap | 34.37 | kPa | 373.27 | Calculated Property |
| Pvap | 140.91 | kPa | 422.05 | Calculated Property |
| Pvap | 413.38 | kPa | 470.83 | Calculated Property |
| Pvap | 971.25 | kPa | 519.61 | Calculated Property |
| Pvap | 1964.29 | kPa | 568.39 | Calculated Property |
| Pvap | 3587.82 | kPa | 617.17 | Calculated Property |
| Pvap | [134.35; 2911.71] | kPa | [420.00; 600.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47489e+01 | |||
| Coefficient B | -3.90294e+03 | |||
| Coefficient C | -2.36980e+01 | |||
| Reference | Ambrose, Broderick, et al., 1967 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 420.00 | |||
| Temperature range, max. | 600.00 | |||
| Pvap | 134.35 | kPa | 420.00 | Calculated Property |
| Pvap | 215.64 | kPa | 440.00 | Calculated Property |
| Pvap | 331.42 | kPa | 460.00 | Calculated Property |
| Pvap | 490.52 | kPa | 480.00 | Calculated Property |
| Pvap | 702.49 | kPa | 500.00 | Calculated Property |
| Pvap | 977.35 | kPa | 520.00 | Calculated Property |
| Pvap | 1325.40 | kPa | 540.00 | Calculated Property |
| Pvap | 1757.03 | kPa | 560.00 | Calculated Property |
| Pvap | 2282.48 | kPa | 580.00 | Calculated Property |
| Pvap | 2911.71 | kPa | 600.00 | Calculated Property |
| Pvap | [6.35; 103.89] | kPa | [329.74; 410.27] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39879e+01 | |||
| Coefficient B | -3.26809e+03 | |||
| Coefficient C | -6.05390e+01 | |||
| Reference | Williamham, Taylor, et al., 1945 | |||
| Temperature range, min. | 329.74 | |||
| Temperature range, max. | 410.27 | |||
| Pvap | 6.35 | kPa | 329.74 | Calculated Property |
| Pvap | 9.38 | kPa | 338.69 | Calculated Property |
| Pvap | 13.53 | kPa | 347.64 | Calculated Property |
| Pvap | 19.08 | kPa | 356.58 | Calculated Property |
| Pvap | 26.38 | kPa | 365.53 | Calculated Property |
| Pvap | 35.80 | kPa | 374.48 | Calculated Property |
| Pvap | 47.77 | kPa | 383.43 | Calculated Property |
| Pvap | 62.76 | kPa | 392.37 | Calculated Property |
| Pvap | 81.29 | kPa | 401.32 | Calculated Property |
| Pvap | 103.89 | kPa | 410.27 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [973.34; 294.64] | kg/m3 | [163.10; 617.20] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.02335e+01 | |||
| Coefficient B | 2.53940e-01 | |||
| Coefficient C | 6.17210e+02 | |||
| Coefficient D | 2.78830e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 163.10 | |||
| Temperature range, max. | 617.20 | |||
| ρl | 973.34 | kg/m3 | 163.10 | Calculated Property |
| ρl | 934.57 | kg/m3 | 213.56 | Calculated Property |
| ρl | 893.89 | kg/m3 | 264.01 | Calculated Property |
| ρl | 850.85 | kg/m3 | 314.47 | Calculated Property |
| ρl | 804.75 | kg/m3 | 364.92 | Calculated Property |
| ρl | 754.54 | kg/m3 | 415.38 | Calculated Property |
| ρl | 698.37 | kg/m3 | 465.83 | Calculated Property |
| ρl | 632.54 | kg/m3 | 516.29 | Calculated Property |
| ρl | 546.96 | kg/m3 | 566.74 | Calculated Property |
| ρl | 294.64 | kg/m3 | 617.20 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 9.55e-04] | N/m | [178.20; 594.05] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.23370e-02 | |||
| Coefficient B | 2.87060e+01 | |||
| Coefficient C | -2.92840e+00 | |||
| Coefficient D | -6.04990e-06 | |||
| Coefficient E | -4.07170e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 594.05 | |||
| γ | 0.04 | N/m | 178.20 | Calculated Property |
| γ | 0.04 | N/m | 224.41 | Calculated Property |
| γ | 0.03 | N/m | 270.61 | Calculated Property |
| γ | 0.03 | N/m | 316.82 | Calculated Property |
| γ | 0.02 | N/m | 363.02 | Calculated Property |
| γ | 0.02 | N/m | 409.23 | Calculated Property |
| γ | 0.01 | N/m | 455.43 | Calculated Property |
| γ | 0.01 | N/m | 501.64 | Calculated Property |
| γ | 0.00 | N/m | 547.84 | Calculated Property |
| γ | 9.55e-04 | N/m | 594.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.00; 0.10] | W/m×K | [178.20; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.59320e-05 | |||
| Coefficient B | 1.32260e+00 | |||
| Coefficient C | 4.86470e+02 | |||
| Coefficient D | 1.43670e+04 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.00 | W/m×K | 178.20 | Calculated Property |
| λ | 0.01 | W/m×K | 269.51 | Calculated Property |
| λ | 0.02 | W/m×K | 360.82 | Calculated Property |
| λ | 0.02 | W/m×K | 452.13 | Calculated Property |
| λ | 0.03 | W/m×K | 543.44 | Calculated Property |
| λ | 0.05 | W/m×K | 634.76 | Calculated Property |
| λ | 0.06 | W/m×K | 726.07 | Calculated Property |
| λ | 0.07 | W/m×K | 817.38 | Calculated Property |
| λ | 0.08 | W/m×K | 908.69 | Calculated Property |
| λ | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.10] | W/m×K | [178.20; 413.10] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | -2.60870e-02 | |||
| Coefficient B | 1.33010e+01 | |||
| Coefficient C | -1.66230e+00 | |||
| Coefficient D | -2.78440e-04 | |||
| Coefficient E | -1.82140e-06 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 413.10 | |||
| λ | 0.16 | W/m×K | 178.20 | Calculated Property |
| λ | 0.15 | W/m×K | 204.30 | Calculated Property |
| λ | 0.15 | W/m×K | 230.40 | Calculated Property |
| λ | 0.14 | W/m×K | 256.50 | Calculated Property |
| λ | 0.13 | W/m×K | 282.60 | Calculated Property |
| λ | 0.13 | W/m×K | 308.70 | Calculated Property |
| λ | 0.12 | W/m×K | 334.80 | Calculated Property |
| λ | 0.11 | W/m×K | 360.90 | Calculated Property |
| λ | 0.11 | W/m×K | 387.00 | Calculated Property |
| λ | 0.10 | W/m×K | 413.10 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, ethyl-.
Mixtures
- Benzene, ethyl- + Methyl Alcohol
- Benzene, nitro- + Benzene, ethyl-
- Benzene, ethyl- + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
- Benzene, ethyl- + 2,4-Pentanedione
- Phenol, 2-methyl- + Benzene, ethyl-
- PHENOL, 4-METHYL- + Benzene, ethyl-
- Benzene, ethyl- + 1-Hexanol
- Benzene, ethyl- + Tetraethyl silicate
- 1,3-Dioxolan-2-one, 4-methyl- + Benzene, ethyl-
- Triethylene glycol + Benzene, ethyl-
- 2-Amino-4-chlorobenzoic acid + Benzene, ethyl-
- Benzene, ethyl- + Cyclohexanone
- Acetic acid, 1,1-dimethylethyl ester + Benzene, ethyl-
- Benzene, ethyl- + 1-Propanone, 1-phenyl-
- Cyclooctane + Benzene, ethyl-
- Benzene, ethyl- + Water
- Benzene, ethyl- + Ethanol, 2-(2-aminoethoxy)- + Water
- Benzene, ethyl- + Methyldiethanolamine + Water
- Morpholine, 4-acetyl- + Benzene, ethyl-
- Benzene, ethyl- + Water + Phosphoric Acid
Find more mixtures with Benzene, ethyl-.
Sources
- KDB Vapor Pressure Data
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
- Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
- Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
- Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
- Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
- Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
- Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
- Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
- Limiting activity coefficients in binary mixtures of 1-alkanols and ethylbenzene
- Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K
- Thermodynamics of dissolution for 1-naphtol N-methylcarbamate in pure, mineral and Mediterranean sea water by dynamic saturation method
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Solubility of pyrene in simple and mixed solvent systems
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Measurement and correlation of liquid liquid equilibria for ternary systems {cyclooctane + aromatic hydrocarbon + 1-ethyl-3-methylpyridinium ethylsulfate} at T = 298.15 K and atmospheric pressure
- (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}
- Liquid-liquid equilibria for ternary systems of {cyclohexane + aromatic compounds + 1-ethyl-3-methylpyridinium ethylsulfate}
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Binary and ternary vapor-liquid equilibrium data of the system ethylbenzene + styrene + 3-methyl-N-butylpyridinium tetracyanoborate at vacuum conditions and liquid-liquid equilibrium data of their binary systems
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- (Liquid + liquid) equilibria for the ternary system of (N-formylmorpholine + ethylbenzene + 2,2,4-trimethylpentane) at temperatures (303.15, 313.15, and 323.15) K
- Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
- Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
- Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
- (Liquid-liquid) equilibria for ternary and quaternary systems of representative compounds of gasoline + methanol at 293.15 K: Experimental data and correlation
- Vapor-liquid equilibria of binary mixtures of propylene oxide witheither ethyl benzene, 2-methylpentane, or 2-methyl-1-pentene
- Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
- Phase equilibria of binary mixtures (ionic liquid + aromatic hydrocarbon): Effect of the structure of the components on the solubility
- Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Extraction of benzene, ethylbenzene, and xylenes from n-heptane using binary mixtures of [4empy][Tf2N] and [emim][DCA] ionic liquids
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
- The ionic liquid 1-ethyl-3-methylimidazolium tris(pentafluoroethyl) trifluorophosphate as alternative extractant for BTEX separation
- Liquid-liquid phase diagrams of poly(ethylene glycol) and aromatic hydrocarbons
- Experimental study on liquid - liquid equilibria of ionic liquids + alkane + ethyl benzene or p-xylene at 298.15 K
- Measurement of infinite dilution partition coefficients of isomeric benzene derivatives in [bmim][Tf2N]-CO2 biphasic system and correlation with the ePC-SAFT equation of state
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- Vapor-liquid equilibria for n-heptane + (benzene, toluene, pxylene, or ethylbenzene) + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} binary ionic liquid mixture
- Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurement and modeling of infinite dilution activity coefficients of organic compounds in an equimolar ionic liquid mixture of [Bmim]Cl and [Bmim][Tf2N]
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
- Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
- Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
- Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
- A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
- Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
- Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
- The (p,q,T) of (methanol + benzene) and (methanol + ethylbenzene)
- The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
- Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
- Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
- Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
- Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
- A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Solubility of ethylbenzene and xylene in pure water and aqueous alkanolamine solutions
- Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
- Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Effect of temperature on the physical properties of two ionic liquids
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
- (Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Thermophysical properties and phase equilibria study of the binary systems {N-hexylquinolinium bis(trifluoromethylsulfonyl)imide + aromatic hydrocarbons, or an alcohol}
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Densities, viscosities, speed of sound, and IR spectroscopic studies of binary mixtures of tert-butyl acetate with benzene, methylbenzene, and ethylbenzene at T = (298.15 and 308.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Binary and ternary LLE data of the system (ethylbenzene + styrene + 1-ethyl-3-methylimidazolium thiocyanate) and binary VLE data of the system (styrene + 1-ethyl-3-methylimidazolium thiocyanate)
- Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- Determination of infinite dilution activity coefficients using HS-SPME/GC/FID for hydrocarbons in furfural at temperatures of (298.15, 308.15, and 318.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
- Liquid-liquid extraction of aromatics from their mixtures with alkanes using 1-methyl 3-octylimidazolium thiocyanate ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
- Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
- Thermodynamics of solvation and solvophobic effect in formamide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
- The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
- (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
- Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Measurements and equation-of-state modelling of thermodynamic properties of binary mixtures of 1-butyl-1-methylpyrrolidinium tetracyanoborate ionic liquid with molecular compounds
- Experimental and correlational study of phase equilibria in aqueous mixtures of phosphoric acid with aromatic hydrocarbons at various temperatures
- Viscosity measurements of ortho-xylene, meta-xylene, para-xylene and ethylbenzene
- The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
- Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
- Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
- Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Liquid-liquid equilibria for the ternary system of water + furfural + solvents at 303.15 and 323.15 K under atmospheric pressure
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Liquid-liquid extraction of styrene from ethylbenzene using ionic liquids
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
- Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
- Liquid Phase Equilibria of Aqueous Mixtures of Carboxylic Acids (C1-C4) with Ethylbenzene: Thermodynamic and Mathematical Modeling
- Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
- Liquid Liquid Equilibria Data for Ethylbenzene or p-Xylene with Alkane and 1-Butylpyridinium Nitrate Ionic Liquid at 298.15 K
- Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
- Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
- Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
- Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
- Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
- Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa
- Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
- Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
- Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
- Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
- High-Temperature VLE for the Ethylbenzene + Quinoline System
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
- Solubility of Alkylbenzenes and a Model for Predicting the Solubility of Liquid Organics in High-Temperature Water
- Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
- Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
- Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
- Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
- Solubility of Hexafluorobenzene in Aqueous Salt Solutions from (280 to 340) K
- Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
- Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15, 313.15, and 323.15) K
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
- Saturated Heat Capacities of Some Linear and Branched Alkylbenzenes between (332 and 401) K
- Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
- Solubilities at High Dilution of Toluene, Ethylbenzene, 1,2,4-Trimethylbenzene, and Hexane in Di-2-ethylhexyl, Diisoheptyl, and Diisononyl Phthalates
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
- Ternary Liquid-Liquid Equilibria for Mixtures of an Aromatic + an Aliphatic Hydrocarbon + 4-Methyl-N-butylpyridinium Tetrafluoroborate
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
- Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Isobaric Vapor-Liquid Equilibium for the Binary Systems of Methyl Formate with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.33 kPa
- Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Binary and Ternary Vapor-Liquid Equilibrium Data of the System (Ethylbenzene + Styrene + 4-Methyl-N-butylpyridinium Tetrafluoroborate) at Vacuum Conditions and Liquid-Liquid Equilibrium Data of Their Binary Systems
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
- Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
- Liquid-Liquid Equilibrium for the Ternary System Water + Ethylbenzene + Acetophenone and Water + Ethylbenzene + 1-Phenylethanol
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
- Solubility of 2,6-Diaminopyridine in Toluene, o-Xylene, Ethylbenzene, Methanol, Ethanol, 2-Propanol, and Sodium Hydroxide Solutions
- Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
- Phase Equilibria of (1-Ethyl-3-methylimidazolium Ethylsulfate + Hydrocarbon, + Ketone, and + Ether) Binary Systems
- Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
- Liquid-Liquid Equilibrium of Ternary Systems of Cyclohexane + (Benzene, + Toluene, + Ethylbenzene, or + o-Xylene) + 4-Methyl-N-butyl Pyridinium Tetrafluoroborate Ionic Liquid at 303.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
- Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
- Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
- Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
- Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.
These property values are available through the Cheméo API. A free account gives you an access key.