- 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
- Benzene, ethyl-
- EB
- Ethylbenzeen
- Ethylbenzol
- Etilbenzene
- Etylobenzen
- NCI-C56393
- NSC 406903
- Phenylethane
- UN 1175
- «alpha»-Methyltoluene
- «alpha»-Methyltoluene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- 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.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- 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 : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3020 | KDB | |
| PAff | [788.00; 789.90] | kJ/mol |
|
| PAff | 788.00 | kJ/mol | NIST |
| PAff | 789.90 | kJ/mol | NIST |
| Tig | 733.15 | K | KDB |
| BasG | [760.20; 760.30] | kJ/mol |
|
| BasG | 760.30 | kJ/mol | NIST |
| BasG | 760.20 | kJ/mol | NIST |
| Cp,liquid | 185.44 | J/mol×K | Thermod... |
| μ | 0.40 | debye | KDB |
| LFL | 1.00 | % in Air | KDB |
| UFL | 6.70 | % in Air | KDB |
| Tflash,cc | 299.82 | K | KDB |
| Tflash,oc | 288.15 | K | KDB |
| 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 | 29.81 | 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° | 35.68 | kJ/mol | Joback Calculated Property |
| 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. Sol... | |
| log10WS | -2.77 | Estimat... | |
| logPoct/wat | 2.249 | Crippen Calculated Property | |
| McVol | 99.820 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 3609.00 | kPa | KDB |
| 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 | 858.00 | NIST | |
| Inp | 845.00 | NIST | |
| I | [1098.00; 1180.00] |
|
|
| 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 | 1125.00 | NIST | |
| I | 1125.00 | 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 | 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 | 1110.00 | NIST | |
| I | 1117.00 | NIST | |
| I | 1120.00 | 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 | [409.25; 409.35] | K |
|
| Tboil | 409.34 | K | KDB |
| Tboil | 409.35 | K | Isobari... |
| Tboil | 409.35 | K | Isobari... |
| Tboil | 409.32 | K | Isobari... |
| Tboil | 409.25 | K | Isobari... |
| Tc | 617.15 | K | KDB |
| Tfus | [178.20; 278.29] | K |
|
| Tfus | 178.20 | K | Aq. Sol... |
| Tfus | 178.20 | K | KDB |
| Tfus | 278.29 | K | Phase E... |
| Ttriple | [178.00; 178.15] | K |
|
| Ttriple | 178.15 ± 0.02 | K | NIST |
| Ttriple | 178.00 ± 0.30 | K | NIST |
| Vc | [0.374; 0.374] | m3/kmol |
|
| Vc | 0.374 | m3/kmol | KDB |
| Vc | 0.374 | m3/kmol | NIST |
| Zc | 0.2630460 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [159.24; 214.02] | J/mol×K | [373.15; 523.15] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 210 400 450 500 | ||||
| Cp,gas | 159.24 ± 0.80 | J/mol×K | 373.15 | NIST |
| Cp,gas | 164.25 ± 0.33 | J/mol×K | 385.65 | NIST |
| Cp,gas | 169.25 ± 0.34 | J/mol×K | 398.15 | NIST |
| Cp,gas | 178.96 ± 0.36 | J/mol×K | 423.15 | NIST |
| Cp,gas | 188.28 ± 0.38 | J/mol×K | 448.15 | NIST |
| Cp,gas | 197.35 ± 0.39 | J/mol×K | 473.15 | NIST |
| Cp,gas | 205.94 ± 0.41 | J/mol×K | 498.15 | NIST |
| Cp,gas | 214.02 ± 0.43 | J/mol×K | 523.15 | NIST |
| Cp,liquid | [161.00; 186.60] | J/mol×K | [293.31; 303.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 160 165 170 175 180 185 295 300 | ||||
| Cp,liquid | 184.80 | J/mol×K | 293.31 | NIST |
| Cp,liquid | 161.00 | J/mol×K | 295.00 | NIST |
| Cp,liquid | 181.60 | J/mol×K | 297.40 | NIST |
| Cp,liquid | 185.80 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 184.50 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 185.78 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 186.04 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 185.56 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 185.81 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 186.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 185.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 183.70 | J/mol×K | 298.50 | NIST |
| Cp,liquid | 178.70 | J/mol×K | 302.70 | NIST |
| Cp,liquid | 178.70 | J/mol×K | 302.80 | NIST |
| Cp,liquid | 181.60 | J/mol×K | 303.00 | NIST |
| η | [0.0003660; 0.0006793] | Pa×s | [293.15; 353.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.50e-4 4.00e-4 4.50e-4 5.00e-4 5.50e-4 6.00e-4 6.50e-4 7.00e-4 300 320 340 | ||||
| η | 0.0006793 | Pa×s | 293.15 | Viscosi... |
| η | 0.0006280 | Pa×s | 298.15 | Viscosi... |
| η | 0.0006299 | Pa×s | 298.15 | Excess ... |
| η | 0.0006380 | Pa×s | 298.15 | Densiti... |
| η | 0.0006006 | Pa×s | 303.15 | Viscosi... |
| η | 0.0005980 | Pa×s | 303.15 | Densiti... |
| η | 0.0005970 | Pa×s | 303.15 | Viscosi... |
| η | 0.0005986 | Pa×s | 303.15 | Densiti... |
| η | 0.0005981 | Pa×s | 303.15 | Excess ... |
| η | 0.0005970 | Pa×s | 303.15 | Thermop... |
| η | 0.0005340 | Pa×s | 308.15 | Densiti... |
| η | 0.0005530 | Pa×s | 308.15 | Viscosi... |
| η | 0.0005652 | Pa×s | 308.15 | Viscome... |
| η | 0.0005691 | Pa×s | 308.15 | Densiti... |
| η | 0.0005380 | Pa×s | 313.15 | Viscosi... |
| η | 0.0005370 | Pa×s | 313.15 | Densiti... |
| η | 0.0005372 | Pa×s | 313.15 | Densiti... |
| η | 0.0005294 | Pa×s | 313.15 | Viscome... |
| η | 0.0005355 | Pa×s | 313.15 | Viscosi... |
| η | 0.0005380 | Pa×s | 313.15 | Thermop... |
| η | 0.0005060 | Pa×s | 318.15 | Densiti... |
| η | 0.0004829 | Pa×s | 323.15 | Excess ... |
| η | 0.0004830 | Pa×s | 323.15 | Densiti... |
| η | 0.0004805 | Pa×s | 323.15 | Densiti... |
| η | 0.0004566 | Pa×s | 328.15 | Densiti... |
| η | 0.0004371 | Pa×s | 333.15 | Densiti... |
| η | 0.0004370 | Pa×s | 333.15 | Densiti... |
| η | 0.0003970 | Pa×s | 343.15 | Densiti... |
| η | 0.0003660 | Pa×s | 353.15 | Densiti... |
| ΔfusH | [9.16; 9.18] | kJ/mol | [178.00; 178.20] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 9.16 9.16 9.17 9.17 9.18 178 178.1 178.20000000000002 | ||||
| ΔfusH | 9.16 | kJ/mol | 178.00 | NIST |
| ΔfusH | 9.18 | kJ/mol | 178.15 | NIST |
| ΔfusH | 9.16 | kJ/mol | 178.17 | NIST |
| ΔfusH | 9.16 | kJ/mol | 178.20 | NIST |
| ΔfusH | 9.16 | kJ/mol | 178.20 | NIST |
| ΔvapH | [35.50; 42.49] | kJ/mol | [294.01; 583.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 300 400 500 | ||||
| ΔvapH | 42.49 | kJ/mol | 294.01 | NIST |
| ΔvapH | 40.50 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 39.50 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 38.60 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 41.80 | kJ/mol | 359.00 | NIST |
| ΔvapH | 40.60 | kJ/mol | 360.00 | NIST |
| ΔvapH | 40.00 | kJ/mol | 370.00 | NIST |
| ΔvapH | 35.56 | kJ/mol | 409.20 | KDB |
| ΔvapH | 35.57 | kJ/mol | 409.30 | NIST |
| ΔvapH | 37.00 | kJ/mol | 434.00 | NIST |
| ΔvapH | 35.80 | kJ/mol | 505.50 | NIST |
| ΔvapH | 35.50 | kJ/mol | 583.00 | NIST |
| Pvap | [2.10; 3451.00] | kPa | [308.15; 613.15] |
|
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 400 500 600 | ||||
| Pvap | 2.22 | kPa | 308.15 | Vapor-l... |
| Pvap | 2.10 | kPa | 313.15 | Vapor-l... |
| Pvap | 3.75 | kPa | 318.15 | Vapor-l... |
| Pvap | 4.08 | kPa | 320.15 | Vapour-... |
| Pvap | 4.71 | kPa | 323.15 | Vapor-l... |
| Pvap | 5.00 | kPa | 324.40 | Isobari... |
| Pvap | 5.41 | kPa | 326.15 | Vapour-... |
| Pvap | 5.97 | kPa | 328.15 | Vapor-l... |
| Pvap | 7.09 | kPa | 332.15 | Vapour-... |
| Pvap | 7.45 | kPa | 333.15 | Vapor-l... |
| Pvap | 7.50 | kPa | 333.40 | Isobari... |
| Pvap | 9.19 | kPa | 338.15 | Vapour-... |
| Pvap | 9.25 | kPa | 338.15 | Vapor-l... |
| Pvap | 10.00 | kPa | 340.00 | Isobari... |
| Pvap | 11.41 | kPa | 343.15 | Vapor-l... |
| Pvap | 11.79 | kPa | 344.15 | Vapour-... |
| Pvap | 12.50 | kPa | 345.50 | Isobari... |
| Pvap | 13.79 | kPa | 348.15 | Vapor-l... |
| Pvap | 15.00 | kPa | 350.10 | Isobari... |
| Pvap | 17.50 | kPa | 354.10 | Isobari... |
| Pvap | 20.00 | kPa | 357.70 | Isobari... |
| Pvap | 20.42 | kPa | 358.15 | Vapor-l... |
| Pvap | 22.50 | kPa | 360.90 | Isobari... |
| Pvap | 25.00 | kPa | 363.80 | Isobari... |
| Pvap | 26.66 | kPa | 365.86 | Isobari... |
| Pvap | 29.11 | kPa | 368.15 | Vapor-l... |
| Pvap | 40.00 | kPa | 377.54 | Determi... |
| Pvap | 47.75 | kPa | 383.15 | Vapor-l... |
| Pvap | 53.33 | kPa | 386.69 | Determi... |
| Pvap | 53.33 | kPa | 386.94 | Isobari... |
| Pvap | 66.66 | kPa | 394.14 | Determi... |
| Pvap | 79.99 | kPa | 400.51 | Determi... |
| Pvap | 79.99 | kPa | 400.70 | Isobari... |
| Pvap | 85.64 | kPa | 403.15 | Vapor-l... |
| Pvap | 93.32 | kPa | 406.12 | Determi... |
| Pvap | 93.13 | kPa | 406.23 | Refract... |
| Pvap | 95.30 | kPa | 406.95 | Vapor-l... |
| Pvap | 250.00 | kPa | 447.20 | Isobari... |
| Pvap | 681.00 | kPa | 498.15 | High-Te... |
| Pvap | 1027.00 | kPa | 523.15 | High-Te... |
| Pvap | 1601.00 | kPa | 553.15 | High-Te... |
| Pvap | 2387.00 | kPa | 583.15 | High-Te... |
| Pvap | 3451.00 | kPa | 613.15 | High-Te... |
| n0 | [1.49020; 1.54395] | [283.15; 303.15] |
|
|
|
T(K) Refractive Index 1.49 1.5 1.51 1.52 1.53 1.54 285 290 295 300 | ||||
| n0 | 1.50129 | 283.15 | Density... | |
| n0 | 1.49620 | 293.10 | Densiti... | |
| n0 | 1.49620 | 293.10 | A study... | |
| n0 | 1.49220 | 293.15 | Volumet... | |
| n0 | 1.49620 | 293.15 | Effect ... | |
| n0 | 1.50090 | 293.15 | Solubil... | |
| n0 | 1.49600 | 293.15 | Activit... | |
| n0 | 1.49570 | 293.15 | Densiti... | |
| n0 | 1.54395 | 293.15 | Bubble ... | |
| n0 | 1.49620 | 293.15 | Experim... | |
| n0 | 1.49550 | 293.15 | Infinit... | |
| n0 | 1.49620 | 293.15 | A study... | |
| n0 | 1.49320 | 298.15 | KDB | |
| n0 | 1.49304 | 298.15 | (Liquid... | |
| n0 | 1.49300 | 298.15 | Experim... | |
| n0 | 1.49620 | 298.15 | Densiti... | |
| n0 | 1.49620 | 298.15 | The vol... | |
| n0 | 1.49304 | 298.15 | Liquid-... | |
| n0 | 1.49310 | 298.15 | Excess ... | |
| n0 | 1.49320 | 298.15 | Isobari... | |
| n0 | 1.49304 | 298.15 | Liquid ... | |
| n0 | 1.49320 | 298.15 | Bubble ... | |
| n0 | 1.49316 | 298.15 | Effect ... | |
| n0 | 1.49304 | 298.15 | Density... | |
| n0 | 1.49304 | 298.15 | Effect ... | |
| n0 | 1.49020 | 303.15 | Densiti... | |
| ρl | [794.20; 875.69] | kg/m3 | [283.15; 373.15] |
|
|
T(K) Liquid Density (kg/m3) 800 820 840 860 880 300 320 340 360 | ||||
| ρl | 875.69 | kg/m3 | 283.15 | The den... |
| ρl | 871.33 | kg/m3 | 288.15 | Thermop... |
| ρl | 871.31 | kg/m3 | 288.15 | Effect ... |
| ρl | 871.30 | kg/m3 | 288.15 | The den... |
| ρl | 867.00 | kg/m3 | 293.00 | KDB |
| ρl | 867.10 | kg/m3 | 293.10 | Vapor-L... |
| ρl | 867.10 | kg/m3 | 293.15 | Densiti... |
| ρl | 866.95 | kg/m3 | 293.15 | Density... |
| ρl | 867.10 | kg/m3 | 293.15 | Densiti... |
| ρl | 866.90 | kg/m3 | 293.15 | The den... |
| ρl | 867.20 | kg/m3 | 293.15 | Densiti... |
| ρl | 866.54 | kg/m3 | 293.15 | Isobari... |
| ρl | 862.58 | kg/m3 | 298.15 | The phy... |
| ρl | 862.50 | kg/m3 | 298.15 | Density... |
| ρl | 862.57 | kg/m3 | 298.15 | Vapor L... |
| ρl | 862.55 | kg/m3 | 298.15 | Excess ... |
| ρl | 862.97 | kg/m3 | 298.15 | Phase b... |
| ρl | 862.59 | kg/m3 | 298.15 | Liquid-... |
| ρl | 862.50 | kg/m3 | 298.15 | Bubble ... |
| ρl | 862.50 | kg/m3 | 298.15 | Thermod... |
| ρl | 862.55 | kg/m3 | 298.15 | Effect ... |
| ρl | 862.43 | kg/m3 | 298.15 | Acousti... |
| ρl | 862.50 | kg/m3 | 298.15 | Excess ... |
| ρl | 862.51 | kg/m3 | 298.15 | Experim... |
| ρl | 862.70 | kg/m3 | 298.15 | Isobari... |
| ρl | 862.51 | kg/m3 | 298.15 | Liquid ... |
| ρl | 862.97 | kg/m3 | 298.15 | Phase b... |
| ρl | 862.51 | kg/m3 | 298.15 | Phase b... |
| ρl | 862.55 | kg/m3 | 298.15 | Thermod... |
| ρl | 862.70 | kg/m3 | 298.15 | Densiti... |
| ρl | 862.70 | kg/m3 | 298.15 | Densiti... |
| ρl | 862.58 | kg/m3 | 298.15 | The den... |
| ρl | 862.57 | kg/m3 | 298.15 | Isobari... |
| ρl | 862.51 | kg/m3 | 298.15 | (Liquid... |
| ρl | 862.37 | kg/m3 | 298.15 | Experim... |
| ρl | 862.59 | kg/m3 | 298.15 | Thermop... |
| ρl | 862.70 | kg/m3 | 298.15 | The den... |
| ρl | 863.54 | kg/m3 | 298.15 | Separat... |
| ρl | 862.50 | kg/m3 | 298.15 | Excess ... |
| ρl | 858.15 | kg/m3 | 303.15 | Density... |
| ρl | 858.10 | kg/m3 | 303.15 | Experim... |
| ρl | 858.30 | kg/m3 | 303.15 | Densiti... |
| ρl | 858.16 | kg/m3 | 303.15 | The den... |
| ρl | 853.61 | kg/m3 | 308.15 | Acousti... |
| ρl | 853.75 | kg/m3 | 308.15 | Effect ... |
| ρl | 853.77 | kg/m3 | 308.15 | Thermop... |
| ρl | 853.80 | kg/m3 | 308.15 | The den... |
| ρl | 853.71 | kg/m3 | 308.15 | The phy... |
| ρl | 853.68 | kg/m3 | 308.15 | Experim... |
| ρl | 849.30 | kg/m3 | 313.15 | Densiti... |
| ρl | 849.29 | kg/m3 | 313.15 | The phy... |
| ρl | 849.29 | kg/m3 | 313.15 | Density... |
| ρl | 849.26 | kg/m3 | 313.15 | Experim... |
| ρl | 844.80 | kg/m3 | 318.15 | The den... |
| ρl | 844.89 | kg/m3 | 318.15 | Thermop... |
| ρl | 844.70 | kg/m3 | 318.15 | The phy... |
| ρl | 844.87 | kg/m3 | 318.15 | Effect ... |
| ρl | 840.28 | kg/m3 | 323.15 | The phy... |
| ρl | 840.30 | kg/m3 | 323.15 | Densiti... |
| ρl | 840.38 | kg/m3 | 323.15 | Density... |
| ρl | 835.94 | kg/m3 | 328.15 | Thermop... |
| ρl | 835.93 | kg/m3 | 328.15 | Effect ... |
| ρl | 831.20 | kg/m3 | 333.15 | Densiti... |
| ρl | 831.40 | kg/m3 | 333.15 | Density... |
| ρl | 822.30 | kg/m3 | 343.15 | Density... |
| ρl | 822.10 | kg/m3 | 343.15 | Densiti... |
| ρl | 813.10 | kg/m3 | 353.15 | Density... |
| ρl | 803.70 | kg/m3 | 363.15 | Density... |
| ρl | 794.20 | kg/m3 | 373.15 | Density... |
| ΔfusS | [51.43; 51.54] | J/mol×K | [178.00; 178.17] |
|
| ΔfusS | 51.48 | J/mol×K | 178.00 | NIST |
| ΔfusS | 51.54 | J/mol×K | 178.15 | NIST |
| ΔfusS | 51.43 | J/mol×K | 178.17 | NIST |
| csound,fluid | [1213.59; 1360.73] | m/s | [288.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1200 1250 1300 1350 290 300 310 320 | ||||
| csound,fluid | 1360.73 | m/s | 288.15 | Influen... |
| csound,fluid | 1359.11 | m/s | 288.15 | Tempera... |
| csound,fluid | 1349.91 | m/s | 290.65 | Influen... |
| csound,fluid | 1340.00 | m/s | 293.15 | Densiti... |
| csound,fluid | 1339.40 | m/s | 293.15 | Influen... |
| csound,fluid | 1328.86 | m/s | 295.65 | Influen... |
| csound,fluid | 1318.36 | m/s | 298.15 | Influen... |
| csound,fluid | 1319.00 | m/s | 298.15 | Densiti... |
| csound,fluid | 1316.23 | m/s | 298.15 | Tempera... |
| csound,fluid | 1307.90 | m/s | 300.65 | Influen... |
| csound,fluid | 1298.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1297.48 | m/s | 303.15 | Influen... |
| csound,fluid | 1287.09 | m/s | 305.65 | Influen... |
| csound,fluid | 1276.75 | m/s | 308.15 | Influen... |
| csound,fluid | 1276.00 | m/s | 308.15 | Densiti... |
| csound,fluid | 1266.54 | m/s | 310.65 | Influen... |
| csound,fluid | 1256.29 | m/s | 313.15 | Influen... |
| csound,fluid | 1257.00 | m/s | 313.15 | Densiti... |
| csound,fluid | 1246.12 | m/s | 315.65 | Influen... |
| csound,fluid | 1236.06 | m/s | 318.15 | Influen... |
| csound,fluid | 1226.09 | m/s | 320.65 | Influen... |
| csound,fluid | 1213.59 | m/s | 323.15 | Tempera... |
| csound,fluid | 1216.34 | m/s | 323.15 | Influen... |
| γ | [0.03; 0.03] | N/m | [293.20; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 300 310 320 | ||||
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 298.15 | Densiti... |
| γ | 0.03 | N/m | 303.15 | Densiti... |
| γ | 0.03 | N/m | 303.15 | Thermo ... |
| γ | 0.03 | N/m | 308.15 | Densiti... |
| γ | 0.03 | N/m | 313.15 | Thermo ... |
| γ | 0.03 | N/m | 323.15 | Thermo ... |
| ΔvapS | 144.50 | J/mol×K | 294.01 | NIST |
| λ | [0.12; 0.14] | W/m×K | [258.00; 329.66] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.13 0.13 0.14 260 280 300 320 | ||||
| λ | 0.14 | W/m×K | 258.00 | Thermal... |
| λ | 0.14 | W/m×K | 258.29 | Thermal... |
| λ | 0.14 | W/m×K | 258.50 | Thermal... |
| λ | 0.13 | W/m×K | 277.34 | Thermal... |
| λ | 0.13 | W/m×K | 277.65 | Thermal... |
| λ | 0.13 | W/m×K | 277.88 | Thermal... |
| λ | 0.13 | W/m×K | 295.86 | Thermal... |
| λ | 0.13 | W/m×K | 296.19 | Thermal... |
| λ | 0.13 | W/m×K | 296.42 | Thermal... |
| λ | 0.12 | W/m×K | 312.38 | Thermal... |
| λ | 0.12 | W/m×K | 312.72 | Thermal... |
| λ | 0.12 | W/m×K | 312.96 | Thermal... |
| λ | 0.12 | W/m×K | 329.05 | Thermal... |
| λ | 0.12 | W/m×K | 329.41 | Thermal... |
| λ | 0.12 | W/m×K | 329.66 | Thermal... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | 408.75 | K | 95.30 | Excess ... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [297.90; 436.98] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| 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 | [4.05e-06; 3587.82] | kPa | [178.15; 617.17] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.97937e+01 | |||
| Coefficient B | -7.63808e+03 | |||
| Coefficient C | -9.55398e+00 | |||
| Coefficient D | 5.65318e-06 | |||
| Temperature range, min. | 178.15 | |||
| Temperature range, max. | 617.17 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 400 600 | ||||
| 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 |
Similar Compounds
Find more compounds similar to Ethylbenzene.
Mixtures
- Acetic acid, butyl ester + Ethylbenzene
- Propane, 2-methoxy-2-methyl- + Ethylbenzene
- n-Hexane + Ethylbenzene
- Toluene + Ethylbenzene
- Ethylbenzene + Heptane
- Benzene + Ethylbenzene
- Cyclooctane + Ethylbenzene
- Ethylbenzene + Ethane, 1,1,2,2-tetrachloro-
- Benzene, 1,3-dimethyl- + Ethylbenzene
- Ethylbenzene + Dimethyl Sulfoxide
- Ethylbenzene + 2-Propanol, 1,1'-[(1-methyl-1,2-ethanediyl)bis(oxy)]bis-
- Ethylbenzene + Cyclohexanone
- Ethylbenzene + Acetophenone
- Ethylbenzene + 1-Pentanol
- 2-Propenenitrile + Ethylbenzene
- N,N-Dimethylacetamide + Ethylbenzene
- Methyl Isobutyl Ketone + Ethylbenzene
- Pyridine, 2-methyl- + Ethylbenzene
- Benzene, nitro- + Ethylbenzene
- Ethylbenzene + 1-Propanone, 1-phenyl-
Find more mixtures with Ethylbenzene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- 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
- 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
- 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
- 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
- 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
- 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
- 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
- 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
- The Yaws Handbook of Vapor Pressure
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