- 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.
- Ip : 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(P) : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- 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 | [0.3010; 0.3040] |
|
|
| ω | 0.3010 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3011 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.3040 | ChemSep v8.3 pure component data Compiled value | |
| 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 Compiled value |
| 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 Compiled value |
| 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 Compiled value |
| 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 | [3607.17; 3740.00] | kPa |
|
| Pc | 3609.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Pc | 3607.17 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3609.41 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 3609.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 Compiled value |
| 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 | |
| Ip | [1098.00; 1180.00] |
|
|
| Ip | 1125.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1100.00 | NIST | |
| Ip | 1105.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1131.90 | NIST | |
| Ip | 1158.90 | NIST | |
| Ip | 1164.30 | NIST | |
| Ip | Outlier 1169.80 | NIST | |
| Ip | Outlier 1175.20 | NIST | |
| Ip | 1136.00 | NIST | |
| Ip | 1160.90 | NIST | |
| Ip | 1158.40 | NIST | |
| Ip | 1159.40 | NIST | |
| Ip | 1127.10 | NIST | |
| Ip | 1111.10 | NIST | |
| Ip | Outlier 1178.00 | NIST | |
| Ip | 1154.00 | NIST | |
| Ip | 1162.00 | NIST | |
| Ip | Outlier 1169.00 | NIST | |
| Ip | 1147.00 | NIST | |
| Ip | 1126.00 | NIST | |
| Ip | 1128.00 | NIST | |
| Ip | 1098.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1134.00 | NIST | |
| Ip | 1146.10 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1131.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1115.00 | NIST | |
| Ip | 1115.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1118.00 | NIST | |
| Ip | 1133.00 | NIST | |
| Ip | Outlier 1168.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1124.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1128.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1132.00 | NIST | |
| Ip | 1107.00 | NIST | |
| Ip | 1133.00 | NIST | |
| Ip | 1135.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1121.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1132.00 | NIST | |
| Ip | 1132.00 | NIST | |
| Ip | 1157.00 | NIST | |
| Ip | Outlier 1168.00 | NIST | |
| Ip | Outlier 1180.00 | NIST | |
| Ip | 1135.00 | NIST | |
| Ip | 1146.00 | NIST | |
| Ip | 1145.00 | NIST | |
| Ip | 1144.00 | NIST | |
| Ip | 1146.00 | NIST | |
| Ip | 1157.00 | NIST | |
| Ip | 1166.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1135.00 | NIST | |
| Ip | 1111.00 | NIST | |
| Ip | 1146.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1142.00 | NIST | |
| Ip | 1139.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1161.00 | NIST | |
| Ip | 1104.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1119.00 | NIST | |
| Ip | 1114.00 | NIST | |
| Ip | 1118.00 | NIST | |
| Ip | 1141.00 | NIST | |
| Ip | 1108.00 | NIST | |
| Ip | 1147.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1126.00 | NIST | |
| Ip | 1135.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1109.00 | NIST | |
| Ip | 1126.00 | NIST | |
| Ip | 1124.00 | NIST | |
| Ip | 1124.00 | NIST | |
| Ip | 1134.00 | NIST | |
| Ip | 1139.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1122.00 | NIST | |
| Ip | 1119.00 | NIST | |
| Ip | 1161.00 | NIST | |
| Ip | 1130.00 | NIST | |
| Ip | 1161.00 | NIST | |
| Ip | 1121.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1127.00 | NIST | |
| Ip | 1125.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1161.00 | NIST | |
| Ip | 1109.00 | NIST | |
| Ip | 1132.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1111.00 | NIST | |
| Ip | 1131.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1132.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1117.00 | NIST | |
| Ip | 1110.00 | NIST | |
| Ip | 1117.00 | NIST | |
| Ip | 1120.00 | NIST | |
| Ip | 1100.00 | NIST | |
| Ip | 1164.30 | NIST | |
| Ip | 1158.40 | NIST | |
| Ip | 1154.00 | NIST | |
| Ip | 1116.00 | NIST | |
| Ip | 1129.00 | NIST | |
| Ip | 1115.00 | NIST | |
| Ip | Outlier 1168.00 | NIST | |
| Ip | 1138.00 | NIST | |
| Ip | 1123.00 | NIST | |
| Ip | 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 Compiled value |
| 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 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Tc | 617.10 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 617.17 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 617.15 | K | ChemSep v8.3 pure component data Compiled value |
| 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 | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 178.20 | K | ChemSep v8.3 pure component data Compiled value |
| 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 | 178.17 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 178.20 | K | ChemSep v8.3 pure component data Compiled value |
| 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 Compiled value | |
| URi | 4.60 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.374; 0.374] | m3/kmol |
|
| Vc | 0.374 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value |
| Vc | 0.374 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.374 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.374 | m3/kmol | KDB |
| Vc | 0.374 | m3/kmol | NIST |
| VCOSTALD | 0.37 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.30 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | [0.2630000; 0.2630460] |
|
|
| Zc | 0.2630000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value | |
| Zc | 0.2630000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2630460 | KDB | |
| Zra | [0.26; 0.26] |
|
|
| Zra | 0.26 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil(P) | 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 Compiled value
|
| 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 | |||
| 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 Compiled value
|
| 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 | |||
| 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 Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.45060e+01 | |||
| Coefficient B | 1.23720e+03 | |||
| Coefficient C | 5.28590e-01 | |||
| Coefficient D | -9.13630e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| 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 Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 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 | |||
| 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 Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.30601e+02 | |||
| Coefficient B | -9.74507e+03 | |||
| Coefficient C | -1.73446e+01 | |||
| Coefficient D | 1.27987e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| 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 Compiled value
|
| 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 | |||
| 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; 0.02] | N/m | [178.15; 409.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 6.13626e-02 | |||
| Coefficient B | -1.09400e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 178.15 | |||
| Temperature range, max. | 409.15 | |||
| γ | 0.04 | N/m | 178.15 | Calculated Property |
| γ | 0.04 | N/m | 203.82 | Calculated Property |
| γ | 0.04 | N/m | 229.48 | Calculated Property |
| γ | 0.03 | N/m | 255.15 | Calculated Property |
| γ | 0.03 | N/m | 280.82 | Calculated Property |
| γ | 0.03 | N/m | 306.48 | Calculated Property |
| γ | 0.03 | N/m | 332.15 | Calculated Property |
| γ | 0.02 | N/m | 357.82 | Calculated Property |
| γ | 0.02 | N/m | 383.48 | Calculated Property |
| γ | 0.02 | N/m | 409.15 | Calculated Property |
| γ | [0.04; 9.55e-04] | N/m | [178.20; 594.05] |
ChemSep v8.3 pure component data Compiled value
|
| 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 | |||
| 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 |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [178.20; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.59320e-05 | |||
| Coefficient B | 1.32260e+00 | |||
| Coefficient C | 4.86470e+02 | |||
| Coefficient D | 1.43670e+04 | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 178.20 | Calculated Property |
| λgas | 0.01 | W/m×K | 269.51 | Calculated Property |
| λgas | 0.02 | W/m×K | 360.82 | Calculated Property |
| λgas | 0.02 | W/m×K | 452.13 | Calculated Property |
| λgas | 0.03 | W/m×K | 543.44 | Calculated Property |
| λgas | 0.05 | W/m×K | 634.76 | Calculated Property |
| λgas | 0.06 | W/m×K | 726.07 | Calculated Property |
| λgas | 0.07 | W/m×K | 817.38 | Calculated Property |
| λgas | 0.08 | W/m×K | 908.69 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.16; 0.10] | W/m×K | [178.20; 413.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid 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 | |||
| Temperature range, min. | 178.20 | |||
| Temperature range, max. | 413.10 | |||
| λliquid | 0.16 | W/m×K | 178.20 | Calculated Property |
| λliquid | 0.15 | W/m×K | 204.30 | Calculated Property |
| λliquid | 0.15 | W/m×K | 230.40 | Calculated Property |
| λliquid | 0.14 | W/m×K | 256.50 | Calculated Property |
| λliquid | 0.13 | W/m×K | 282.60 | Calculated Property |
| λliquid | 0.13 | W/m×K | 308.70 | Calculated Property |
| λliquid | 0.12 | W/m×K | 334.80 | Calculated Property |
| λliquid | 0.11 | W/m×K | 360.90 | Calculated Property |
| λliquid | 0.11 | W/m×K | 387.00 | Calculated Property |
| λliquid | 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
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 ChEDL chemicals 1.5.2, from Tsonopoulos, C.; Ambrose, D. Vapor-Liquid Critical Properties of Elements and Compounds. 3. Aromatic Hydrocarbons. J. Chem. Eng. Data 1995, 40, 547-558.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- 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
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