- InChI
- InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
- InChI Key
- CTQNGGLPUBDAKN-UHFFFAOYSA-N
- Formula
- C8H10
- SMILES
- Cc1ccccc1C
- Molecular Weight1
- 106.17
- CAS
- 95-47-6
- Other Names
-
- 1,2-dimethyl-benzene ( o-xylene)
- 1,2-dimethylbenzene
- 1,2-xylene
- 2-Methyltoluene
- 3,4-Xylene
- Benzene, 1,2-dimethyl-
- NSC 60920
- o-Dimethylbenzene
- o-Methyltoluene
- o-Xylol
- ortho-xylene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- SProt : Protonation entropy at 298K (J/mol×K).
- 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).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3100; 0.3120] |
|
|
| ω | 0.3120 | ChemSep v8.3 pure component data | |
| ω | 0.3100 | KDB | |
| PAff | [791.20; 796.00] | kJ/mol |
|
| PAff | 796.00 | kJ/mol | NIST |
| PAff | 791.20 | kJ/mol | NIST |
| PAff | 793.50 ± 1.70 | kJ/mol | NIST |
| Tig | [736.15; 738.15] | K |
|
| Tig | 738.15 | K | KDB |
| Tig | 736.15 | K | NCMS SOLV-DB |
| BasG | [765.30; 772.10] | kJ/mol |
|
| BasG | 768.30 | kJ/mol | NIST |
| BasG | 765.30 | kJ/mol | NIST |
| BasG | 772.10 ± 2.20 | kJ/mol | NIST |
| ΔcH°liquid | [-4581.40; -4551.48] | kJ/mol |
|
| ΔcH°liquid | -4551.48 ± 0.50 | kJ/mol | NIST |
| ΔcH°liquid | -4552.90 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -4567.60 | kJ/mol | NIST |
| ΔcH°liquid | -4581.40 | kJ/mol | NIST |
| Cp,liquid | 187.28 | J/mol×K | Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile) |
| μ | [0.50; 0.63] | debye |
|
| μ | 0.63 | debye | ChemSep v8.3 pure component data |
| μ | 0.50 | debye | KDB |
| η | [0.0007680; 0.0007690] | Pa×s |
|
| η | 0.0007680 | Pa×s | Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K |
| η | 0.0007690 | Pa×s | Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K |
| SProt | 36.90 | J/mol×K | NIST |
| εr | 2.57 | NCMS SOLV-DB | |
| LFL | 1.10 | % in Air | KDB |
| UFL | 7.00 | % in Air | KDB |
| Tflash,cc | [290.15; 297.04] | K |
|
| Tflash,cc | 297.04 | K | KDB |
| Tflash,cc | 290.15 | K | NCMS SOLV-DB |
| Tflash,oc | 290.37 | K | KDB |
| ΔfG° | [122.00; 122.20] | kJ/mol |
|
| ΔfG° | 122.00 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | 122.20 | kJ/mol | KDB |
| Rg | 3.7890 | KDB | |
| Δc,grossH | 4552.86 | kJ/mol | KDB |
| Δc,netH | 4332.784 | kJ/mol | KDB |
| ΔfH°gas | [19.00; 19.08] | kJ/mol |
|
| ΔfH°gas | 19.08 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | 19.00 | kJ/mol | KDB |
| ΔfH°gas | 19.00 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -24.40 ± 1.10 | kJ/mol | NIST |
| ΔfusH° | 10.13 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [36.80; 43.96] | kJ/mol |
|
| ΔvapH° | 43.43 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 43.45 | kJ/mol | NIST |
| ΔvapH° | 42.90 | kJ/mol | NIST |
| ΔvapH° | 43.40 | kJ/mol | NIST |
| ΔvapH° | 43.96 | kJ/mol | NIST |
| ΔvapH° | 36.90 | kJ/mol | NIST |
| ΔvapH° | 43.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 43.43 | kJ/mol | NIST |
| ΔvapH° | 43.40 | kJ/mol | NIST |
| ΔvapH° | Outlier 36.80 ± 0.40 | kJ/mol | NIST |
| IE | [8.45; 8.85] | eV |
|
| IE | 8.56 ± 0.04 | eV | NIST |
| IE | 8.56 ± 0.01 | eV | NIST |
| IE | Outlier 8.85 ± 0.05 | eV | NIST |
| IE | 8.45 ± 0.02 | eV | NIST |
| IE | 8.70 | eV | NIST |
| IE | 8.60 ± 0.10 | eV | NIST |
| IE | 8.61 | eV | NIST |
| IE | 8.55 | eV | NIST |
| IE | 8.56 ± 0.01 | eV | NIST |
| IE | 8.56 ± 0.02 | eV | NIST |
| IE | 8.58 ± 0.01 | eV | NIST |
| IE | 8.56 | eV | NIST |
| IE | 8.57 ± 0.03 | eV | NIST |
| IE | 8.57 | eV | NIST |
| IE | 8.75 ± 0.03 | eV | NIST |
| log10WS | [-2.80; -2.80] |
|
|
| log10WS | -2.80 | Aq. Solubility Prediction | |
| log10WS | -2.80 | Estimated Solubility | |
| logPoct/wat | 3.120 | 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 | [3191.74; 4006.15] | kPa |
|
| Pc | 3732.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 3732.00 | kPa | KDB |
| Pc | 3730.00 ± 40.00 | kPa | NIST |
| Pc | 3731.80 ± 5.00 | kPa | NIST |
| Pc | 3754.00 ± 10.34 | kPa | NIST |
| Pc | 3808.10 ± 80.00 | kPa | NIST |
| Pc | 4006.15 ± 6.00 | kPa | NIST |
| Pc | Outlier 3191.74 ± 1.50 | kPa | NIST |
| Pc | 3620.00 ± 9.81 | kPa | NIST |
| Ptriple | 0.02 | kPa | ChemSep v8.3 pure component data |
| ρc | [286.54; 287.71] | kg/m3 |
|
| ρc | 286.65 ± 4.25 | kg/m3 | NIST |
| ρc | 286.54 ± 5.31 | kg/m3 | NIST |
| ρc | 287.71 ± 4.25 | kg/m3 | NIST |
| Inp | [128.10; 933.00] |
|
|
| Inp | 879.40 | NIST | |
| Inp | 874.60 | NIST | |
| Inp | 875.70 | NIST | |
| Inp | 873.40 | NIST | |
| Inp | 871.90 | NIST | |
| Inp | 874.20 | NIST | |
| Inp | 878.70 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 908.30 | NIST | |
| Inp | 915.10 | NIST | |
| Inp | 874.17 | NIST | |
| Inp | 874.10 | NIST | |
| Inp | 874.64 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 870.90 | NIST | |
| Inp | 873.80 | NIST | |
| Inp | 876.70 | NIST | |
| Inp | 879.50 | NIST | |
| Inp | 882.40 | NIST | |
| Inp | 885.20 | NIST | |
| Inp | 877.40 | NIST | |
| Inp | 878.32 | NIST | |
| Inp | 890.30 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 892.90 | NIST | |
| Inp | 877.60 | NIST | |
| Inp | 877.80 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.10 | NIST | |
| Inp | 877.40 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 889.80 | NIST | |
| Inp | 895.60 | NIST | |
| Inp | 888.80 | NIST | |
| Inp | 888.80 | NIST | |
| Inp | 889.80 | NIST | |
| Inp | 887.30 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 879.60 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 868.30 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 868.40 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 877.60 | NIST | |
| Inp | 878.10 | NIST | |
| Inp | 882.20 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 844.00 | NIST | |
| Inp | 880.80 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 890.30 | NIST | |
| Inp | 896.40 | NIST | |
| Inp | 903.20 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 868.90 | NIST | |
| Inp | 880.30 | NIST | |
| Inp | 880.50 | NIST | |
| Inp | 880.80 | NIST | |
| Inp | 881.50 | NIST | |
| Inp | 875.60 | NIST | |
| Inp | 875.90 | NIST | |
| Inp | 879.90 | NIST | |
| Inp | 880.80 | NIST | |
| Inp | 874.30 | NIST | |
| Inp | 874.50 | NIST | |
| Inp | 880.80 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 877.26 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 878.90 | NIST | |
| Inp | 883.70 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 870.70 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 888.40 | NIST | |
| Inp | 888.10 | NIST | |
| Inp | 880.10 | NIST | |
| Inp | 864.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 918.00 | NIST | |
| Inp | 926.00 | NIST | |
| Inp | 933.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 908.00 | NIST | |
| Inp | 893.20 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 883.80 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 881.80 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 889.90 | NIST | |
| Inp | 891.20 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 898.40 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 877.70 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 892.10 | NIST | |
| Inp | 867.90 | NIST | |
| Inp | 872.30 | NIST | |
| Inp | 876.70 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 889.90 | NIST | |
| Inp | 891.20 | NIST | |
| Inp | 875.31 | NIST | |
| Inp | 875.68 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.88 | NIST | |
| Inp | 875.89 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 881.30 | NIST | |
| Inp | 875.60 | NIST | |
| Inp | 874.60 | NIST | |
| Inp | 870.77 | NIST | |
| Inp | 874.14 | NIST | |
| Inp | 876.31 | NIST | |
| Inp | 887.70 | NIST | |
| Inp | 891.29 | NIST | |
| Inp | 893.63 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 875.12 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 897.40 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 903.66 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 865.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 838.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 899.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 902.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 877.74 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 860.00 | NIST | |
| Inp | 896.50 | NIST | |
| Inp | 850.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 875.60 | NIST | |
| Inp | 870.50 | NIST | |
| Inp | 873.40 | NIST | |
| Inp | 877.30 | NIST | |
| Inp | 880.10 | NIST | |
| Inp | 882.50 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 854.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 869.52 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 901.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 906.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 855.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 888.20 | NIST | |
| Inp | 896.40 | NIST | |
| Inp | 894.90 | NIST | |
| Inp | 894.80 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | Outlier 128.10 | NIST | |
| Inp | Outlier 128.40 | NIST | |
| Inp | Outlier 130.67 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 889.90 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 872.30 | NIST | |
| Inp | 875.88 | NIST | |
| Inp | 881.30 | NIST | |
| Inp | 876.31 | NIST | |
| Inp | 875.12 | NIST | |
| Inp | 883.80 | NIST | |
| I | [1155.00; 1234.30] |
|
|
| I | 1221.00 | NIST | |
| I | Outlier 1234.30 | NIST | |
| I | 1174.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1174.60 | NIST | |
| I | 1188.70 | NIST | |
| I | 1191.40 | NIST | |
| I | 1193.00 | NIST | |
| I | 1200.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1209.84 | NIST | |
| I | 1215.66 | NIST | |
| I | 1221.09 | NIST | |
| I | 1192.98 | NIST | |
| I | 1198.32 | NIST | |
| I | 1204.40 | NIST | |
| I | 1185.70 | NIST | |
| I | 1191.00 | NIST | |
| I | 1183.90 | NIST | |
| I | 1164.90 | NIST | |
| I | Outlier 1230.00 | NIST | |
| I | Outlier 1232.00 | NIST | |
| I | 1210.00 | NIST | |
| I | 1218.00 | NIST | |
| I | Outlier 1227.00 | NIST | |
| I | 1201.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1185.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1195.00 | NIST | |
| I | 1159.00 | NIST | |
| I | 1204.40 | NIST | |
| I | 1187.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1169.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1176.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1193.00 | NIST | |
| I | 1208.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1216.00 | NIST | |
| I | Outlier 1229.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1203.00 | NIST | |
| I | 1202.00 | NIST | |
| I | 1198.00 | NIST | |
| I | 1201.00 | NIST | |
| I | 1213.00 | NIST | |
| I | Outlier 1225.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1159.00 | NIST | |
| I | 1177.00 | NIST | |
| I | 1189.00 | NIST | |
| I | 1197.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1181.00 | NIST | |
| I | 1174.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1192.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1181.00 | NIST | |
| I | Outlier 1155.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1187.00 | NIST | |
| I | Outlier 1225.00 | NIST | |
| I | 1172.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1163.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1175.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1188.00 | NIST | |
| I | 1165.00 | NIST | |
| I | Outlier 1232.00 | NIST | |
| I | 1186.00 | NIST | |
| I | 1183.00 | NIST | |
| I | 1183.00 | NIST | |
| I | Outlier 1232.00 | NIST | |
| I | 1171.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1180.00 | NIST | |
| I | 1190.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1182.00 | NIST | |
| I | 1187.00 | NIST | |
| I | 1165.00 | NIST | |
| I | Outlier 1232.00 | NIST | |
| I | 1191.00 | NIST | |
| I | 1184.00 | NIST | |
| I | 1178.00 | NIST | |
| I | 1204.00 | NIST | |
| I | 1173.00 | NIST | |
| I | 1192.00 | NIST | |
| S°gas | 353.60 ± 1.30 | J/mol×K | NIST |
| S°liquid | [246.02; 248.10] | J/mol×K |
|
| S°liquid | 246.02 | J/mol×K | NIST |
| S°liquid | 248.10 | J/mol×K | NIST |
| Tboil | [414.30; 417.90] | K |
|
| Tboil | 417.50 | K | Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa |
| Tboil | 417.43 | K | Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa |
| Tboil | 417.55 | K | Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa |
| Tboil | 417.56 | 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 | 417.59 | K | ChemSep v8.3 pure component data |
| Tboil | 417.60 | K | KDB |
| Tboil | 417.58 | K | NCMS SOLV-DB |
| Tboil | 417.25 ± 0.30 | K | NIST |
| Tboil | 417.60 | K | NIST |
| Tboil | 417.60 | K | NIST |
| Tboil | 417.60 ± 0.30 | K | NIST |
| Tboil | 417.40 ± 0.70 | K | NIST |
| Tboil | 417.56 ± 0.20 | K | NIST |
| Tboil | 417.60 ± 0.20 | K | NIST |
| Tboil | 417.55 ± 0.15 | K | NIST |
| Tboil | 417.10 ± 0.80 | K | NIST |
| Tboil | 417.55 ± 0.30 | K | NIST |
| Tboil | 417.56 ± 0.30 | K | NIST |
| Tboil | 417.55 ± 0.50 | K | NIST |
| Tboil | 417.90 ± 0.15 | K | NIST |
| Tboil | 417.00 ± 3.00 | K | NIST |
| Tboil | 417.15 ± 0.70 | K | NIST |
| Tboil | 417.65 ± 2.00 | K | NIST |
| Tboil | 417.61 ± 0.25 | K | NIST |
| Tboil | 417.60 ± 0.60 | K | NIST |
| Tboil | 417.56 ± 0.02 | K | NIST |
| Tboil | 416.90 ± 1.00 | K | NIST |
| Tboil | 417.55 ± 0.30 | K | NIST |
| Tboil | 417.61 ± 0.20 | K | NIST |
| Tboil | 417.61 ± 0.20 | K | NIST |
| Tboil | 417.56 ± 0.01 | K | NIST |
| Tboil | 417.56 ± 0.25 | K | NIST |
| Tboil | 417.40 ± 1.00 | K | NIST |
| Tboil | 417.60 ± 0.20 | K | NIST |
| Tboil | Outlier 415.15 ± 0.50 | K | NIST |
| Tboil | 417.57 ± 0.06 | K | NIST |
| Tboil | 417.60 ± 0.20 | K | NIST |
| Tboil | 417.56 ± 0.15 | K | NIST |
| Tboil | 417.55 ± 0.40 | K | NIST |
| Tboil | 417.45 ± 0.30 | K | NIST |
| Tboil | 417.65 ± 0.20 | K | NIST |
| Tboil | 417.15 ± 1.50 | K | NIST |
| Tboil | 417.55 ± 0.10 | K | NIST |
| Tboil | 417.65 ± 0.20 | K | NIST |
| Tboil | 417.20 ± 0.20 | K | NIST |
| Tboil | 417.55 ± 0.50 | K | NIST |
| Tboil | 417.25 ± 0.40 | K | NIST |
| Tboil | 416.85 ± 0.60 | K | NIST |
| Tboil | 417.20 ± 0.25 | K | NIST |
| Tboil | 415.85 ± 0.30 | K | NIST |
| Tboil | 415.55 ± 0.40 | K | NIST |
| Tboil | Outlier 415.00 ± 3.00 | K | NIST |
| Tboil | 417.15 ± 0.40 | K | NIST |
| Tboil | Outlier 415.00 ± 3.00 | K | NIST |
| Tboil | Outlier 415.00 ± 2.00 | K | NIST |
| Tboil | 415.75 ± 0.50 | K | NIST |
| Tboil | 416.00 ± 2.00 | K | NIST |
| Tboil | Outlier 414.30 ± 1.50 | K | NIST |
| Tc | [617.45; 636.10] | K |
|
| Tc | 630.30 | K | ChemSep v8.3 pure component data |
| Tc | 630.30 | K | KDB |
| Tc | 630.30 ± 0.50 | K | NIST |
| Tc | 630.33 ± 0.10 | K | NIST |
| Tc | 629.40 ± 0.50 | K | NIST |
| Tc | 631.59 ± 1.50 | K | NIST |
| Tc | 629.40 ± 1.00 | K | NIST |
| Tc | 630.30 ± 0.60 | K | NIST |
| Tc | 631.00 ± 2.00 | K | NIST |
| Tc | Outlier 617.45 ± 1.50 | K | NIST |
| Tc | 631.10 ± 0.80 | K | NIST |
| Tc | 631.70 ± 2.00 | K | NIST |
| Tc | 636.10 ± 6.00 | K | NIST |
| Tc | 631.50 ± 1.50 | K | NIST |
| Tfus | [228.20; 248.20] | K |
|
| Tfus | 247.98 | K | ChemSep v8.3 pure component data |
| Tfus | 247.90 | K | KDB |
| Tfus | 248.08 | K | Aq. Solubility Prediction |
| Tfus | 247.97 | K | NCMS SOLV-DB |
| Tfus | 248.20 ± 0.50 | K | NIST |
| Tfus | 247.85 ± 0.50 | K | NIST |
| Tfus | 247.92 ± 0.50 | K | NIST |
| Tfus | 245.15 ± 1.50 | K | NIST |
| Tfus | 247.92 ± 0.20 | K | NIST |
| Tfus | 247.92 ± 0.01 | K | NIST |
| Tfus | 247.93 ± 0.10 | K | NIST |
| Tfus | 248.03 ± 0.06 | K | NIST |
| Tfus | 248.15 ± 2.00 | K | NIST |
| Tfus | 248.15 ± 0.25 | K | NIST |
| Tfus | 247.90 ± 0.60 | K | NIST |
| Tfus | 245.20 ± 0.20 | K | NIST |
| Tfus | Outlier 228.20 ± 0.50 | K | NIST |
| Ttriple | [247.80; 247.98] | K |
|
| Ttriple | 247.98 | K | ChemSep v8.3 pure component data |
| Ttriple | 247.80 ± 0.25 | K | NIST |
| Ttriple | 247.80 ± 0.25 | K | NIST |
| UQi | 3.54 | ChemSep v8.3 pure component data | |
| URi | 4.66 | ChemSep v8.3 pure component data | |
| Vc | [0.370; 0.370] | m3/kmol |
|
| Vc | 0.370 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.370 | m3/kmol | KDB |
| Vc | 0.370 | m3/kmol | NIST |
| Zc | [0.2630000; 0.2634870] |
|
|
| Zc | 0.2630000 | ChemSep v8.3 pure component data | |
| Zc | 0.2634870 | KDB | |
| Zra | [0.26; 0.26] |
|
|
| Zra | 0.26 | ChemSep v8.3 pure component data | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 273.48 | 100.00 | 0.0011 |
| 273.48 | 1000.00 | 0.0011 |
| 273.48 | 5000.00 | 0.0012 |
| 273.48 | 10000.00 | 0.0012 |
| 273.48 | 15000.00 | 0.0013 |
| 273.48 | 20000.00 | 0.0013 |
| 273.48 | 25000.00 | 0.0014 |
| 273.48 | 30000.00 | 0.0014 |
| 283.22 | 100.00 | 0.0009 |
| 283.22 | 1000.00 | 0.0010 |
| 283.22 | 5000.00 | 0.0010 |
| 283.21 | 10000.00 | 0.0010 |
| 283.21 | 15000.00 | 0.0011 |
| 283.21 | 20000.00 | 0.0011 |
| 283.21 | 25000.00 | 0.0012 |
| 283.21 | 30000.00 | 0.0012 |
| 293.04 | 100.00 | 0.0008 |
| 293.04 | 1000.00 | 0.0008 |
| 293.04 | 5000.00 | 0.0009 |
| 293.04 | 10000.00 | 0.0009 |
| 293.05 | 15000.00 | 0.0009 |
| 293.05 | 20000.00 | 0.0010 |
| 293.05 | 25000.00 | 0.0010 |
| 293.06 | 30000.00 | 0.0010 |
| 302.87 | 100.00 | 0.0007 |
| 302.87 | 1000.00 | 0.0007 |
| 302.88 | 5000.00 | 0.0007 |
| 302.88 | 10000.00 | 0.0008 |
| 302.88 | 15000.00 | 0.0008 |
| 302.87 | 20000.00 | 0.0008 |
| 302.87 | 25000.00 | 0.0009 |
| 302.87 | 30000.00 | 0.0009 |
| 312.66 | 100.00 | 0.0006 |
| 312.67 | 1000.00 | 0.0006 |
| 312.67 | 5000.00 | 0.0007 |
| 312.66 | 10000.00 | 0.0007 |
| 312.67 | 15000.00 | 0.0007 |
| 312.66 | 20000.00 | 0.0007 |
| 312.66 | 25000.00 | 0.0008 |
| 312.66 | 30000.00 | 0.0008 |
| 321.85 | 100.00 | 0.0006 |
| 321.85 | 1000.00 | 0.0006 |
| 321.86 | 5000.00 | 0.0006 |
| 321.85 | 10000.00 | 0.0006 |
| 321.85 | 15000.00 | 0.0006 |
| 321.86 | 20000.00 | 0.0007 |
| 321.86 | 25000.00 | 0.0007 |
| 321.85 | 30000.00 | 0.0007 |
| 332.47 | 100.00 | 0.0005 |
| 332.47 | 1000.00 | 0.0005 |
| 332.48 | 5000.00 | 0.0005 |
| 332.48 | 10000.00 | 0.0006 |
| 332.48 | 15000.00 | 0.0006 |
| 332.48 | 20000.00 | 0.0006 |
| 332.48 | 25000.00 | 0.0006 |
| 332.48 | 30000.00 | 0.0007 |
| 343.06 | 100.00 | 0.0005 |
| 343.07 | 1000.00 | 0.0005 |
| 343.07 | 5000.00 | 0.0005 |
| 343.07 | 10000.00 | 0.0005 |
| 343.08 | 15000.00 | 0.0005 |
| 343.09 | 20000.00 | 0.0005 |
| 343.08 | 25000.00 | 0.0006 |
| 343.08 | 30000.00 | 0.0006 |
| 353.04 | 100.00 | 0.0004 |
| 353.04 | 1000.00 | 0.0004 |
| 353.03 | 5000.00 | 0.0004 |
| 353.02 | 10000.00 | 0.0005 |
| 353.02 | 15000.00 | 0.0005 |
| 353.02 | 20000.00 | 0.0005 |
| 353.02 | 25000.00 | 0.0005 |
| 353.01 | 30000.00 | 0.0005 |
| 362.85 | 100.00 | 0.0004 |
| 362.85 | 1000.00 | 0.0004 |
| 362.85 | 5000.00 | 0.0004 |
| 362.85 | 10000.00 | 0.0004 |
| 362.86 | 15000.00 | 0.0004 |
| 362.86 | 20000.00 | 0.0005 |
| 362.87 | 25000.00 | 0.0005 |
| 362.87 | 30000.00 | 0.0005 |
| 372.83 | 100.00 | 0.0004 |
| 372.84 | 1000.00 | 0.0004 |
| 372.84 | 5000.00 | 0.0004 |
| 372.85 | 10000.00 | 0.0004 |
| 372.86 | 15000.00 | 0.0004 |
| 372.86 | 20000.00 | 0.0004 |
| 372.85 | 25000.00 | 0.0004 |
| 372.86 | 30000.00 | 0.0004 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0007 |
| Reference | ||
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 93.00 | 298.15 | 1.5022 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 890.5 |
| 283.15 | 1000.00 | 890.8 |
| 283.15 | 3000.00 | 892.4 |
| 283.15 | 5000.00 | 893.5 |
| 283.15 | 10000.00 | 896.7 |
| 283.15 | 15000.00 | 899.0 |
| 283.15 | 20000.00 | 902.6 |
| 283.15 | 25000.00 | 905.3 |
| 283.15 | 30000.00 | 908.1 |
| 283.15 | 35000.00 | 910.9 |
| 283.15 | 40000.00 | 913.3 |
| 283.15 | 50000.00 | 918.2 |
| 283.15 | 60000.00 | 923.0 |
| 293.15 | 100.00 | 879.7 |
| 293.15 | 1000.00 | 879.9 |
| 293.15 | 3000.00 | 881.4 |
| 293.15 | 5000.00 | 882.4 |
| 293.15 | 10000.00 | 885.9 |
| 293.15 | 15000.00 | 888.9 |
| 293.15 | 20000.00 | 892.0 |
| 293.15 | 25000.00 | 894.9 |
| 293.15 | 30000.00 | 897.8 |
| 293.15 | 35000.00 | 900.5 |
| 293.15 | 40000.00 | 903.1 |
| 293.15 | 50000.00 | 908.5 |
| 293.15 | 60000.00 | 913.1 |
| 303.15 | 100.00 | 870.9 |
| 303.15 | 1000.00 | 871.6 |
| 303.15 | 3000.00 | 873.0 |
| 303.15 | 5000.00 | 874.4 |
| 303.15 | 10000.00 | 877.8 |
| 303.15 | 15000.00 | 881.1 |
| 303.15 | 20000.00 | 884.2 |
| 303.15 | 25000.00 | 887.3 |
| 303.15 | 30000.00 | 890.3 |
| 303.15 | 35000.00 | 893.1 |
| 303.15 | 40000.00 | 895.9 |
| 303.15 | 50000.00 | 901.2 |
| 303.15 | 60000.00 | 906.4 |
| 313.15 | 100.00 | 862.7 |
| 313.15 | 1000.00 | 862.9 |
| 313.15 | 3000.00 | 864.5 |
| 313.15 | 5000.00 | 865.9 |
| 313.15 | 10000.00 | 869.6 |
| 313.15 | 15000.00 | 873.0 |
| 313.15 | 20000.00 | 876.3 |
| 313.15 | 25000.00 | 879.6 |
| 313.15 | 30000.00 | 882.7 |
| 313.15 | 35000.00 | 885.7 |
| 313.15 | 40000.00 | 888.4 |
| 313.15 | 50000.00 | 894.2 |
| 313.15 | 60000.00 | 899.2 |
| 323.15 | 100.00 | 853.8 |
| 323.15 | 1000.00 | 854.6 |
| 323.15 | 3000.00 | 856.1 |
| 323.15 | 5000.00 | 857.7 |
| 323.15 | 10000.00 | 861.5 |
| 323.15 | 15000.00 | 865.2 |
| 323.15 | 20000.00 | 868.8 |
| 323.15 | 25000.00 | 872.0 |
| 323.15 | 30000.00 | 875.3 |
| 323.15 | 35000.00 | 878.4 |
| 323.15 | 40000.00 | 881.5 |
| 323.15 | 50000.00 | 887.3 |
| 323.15 | 60000.00 | 892.8 |
| 333.15 | 100.00 | 845.1 |
| 333.15 | 1000.00 | 846.0 |
| 333.15 | 3000.00 | 847.8 |
| 333.15 | 5000.00 | 849.4 |
| 333.15 | 10000.00 | 853.3 |
| 333.15 | 15000.00 | 857.1 |
| 333.15 | 20000.00 | 860.9 |
| 333.15 | 25000.00 | 864.4 |
| 333.15 | 30000.00 | 867.8 |
| 333.15 | 35000.00 | 871.0 |
| 333.15 | 40000.00 | 874.3 |
| 333.15 | 50000.00 | 880.3 |
| 333.15 | 60000.00 | 886.0 |
| 343.15 | 100.00 | 836.3 |
| 343.15 | 1000.00 | 837.2 |
| 343.15 | 3000.00 | 839.0 |
| 343.15 | 5000.00 | 840.9 |
| 343.15 | 10000.00 | 844.9 |
| 343.15 | 15000.00 | 849.0 |
| 343.15 | 20000.00 | 853.0 |
| 343.15 | 25000.00 | 856.6 |
| 343.15 | 30000.00 | 860.2 |
| 343.15 | 35000.00 | 863.7 |
| 343.15 | 40000.00 | 866.8 |
| 343.15 | 50000.00 | 873.2 |
| 343.15 | 60000.00 | 878.9 |
| 353.15 | 100.00 | 827.8 |
| 353.15 | 1000.00 | 828.6 |
| 353.15 | 3000.00 | 830.6 |
| 353.15 | 5000.00 | 832.4 |
| 353.15 | 10000.00 | 836.9 |
| 353.15 | 15000.00 | 841.2 |
| 353.15 | 20000.00 | 845.1 |
| 353.15 | 25000.00 | 849.1 |
| 353.15 | 30000.00 | 852.8 |
| 353.15 | 35000.00 | 856.4 |
| 353.15 | 40000.00 | 859.8 |
| 353.15 | 50000.00 | 866.3 |
| 353.15 | 60000.00 | 872.5 |
| 363.15 | 100.00 | 819.3 |
| 363.15 | 1000.00 | 820.3 |
| 363.15 | 3000.00 | 822.4 |
| 363.15 | 5000.00 | 824.3 |
| 363.15 | 10000.00 | 828.7 |
| 363.15 | 15000.00 | 833.6 |
| 363.15 | 20000.00 | 837.6 |
| 363.15 | 25000.00 | 841.5 |
| 363.15 | 30000.00 | 845.5 |
| 363.15 | 35000.00 | 849.3 |
| 363.15 | 40000.00 | 853.1 |
| 363.15 | 50000.00 | 859.8 |
| 363.15 | 60000.00 | 866.3 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [96.11; 359.49] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.39860e+01 | |||
| Coefficient B | -5.89130e+02 | |||
| Coefficient C | 6.02824e+00 | |||
| Coefficient D | 8.01220e-05 | |||
| Coefficient E | -4.50740e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 96.11 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 150.70 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 201.93 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 243.12 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 275.50 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 300.99 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 321.17 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 337.14 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 349.72 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 359.49 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [173.84; 233.12] | J/mol×K | [247.80; 473.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.34490e+02 | |||
| Coefficient B | -1.70610e+02 | |||
| Coefficient C | 3.33924e+00 | |||
| Coefficient D | 4.90960e-03 | |||
| Coefficient E | -3.17270e-06 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 247.80 | |||
| Temperature range, max. | 473.15 | |||
| Cp,liquid | 173.84 | J/mol×K | 247.80 | Calculated Property |
| Cp,liquid | 179.97 | J/mol×K | 272.84 | Calculated Property |
| Cp,liquid | 186.29 | J/mol×K | 297.88 | Calculated Property |
| Cp,liquid | 192.78 | J/mol×K | 322.92 | Calculated Property |
| Cp,liquid | 199.41 | J/mol×K | 347.96 | Calculated Property |
| Cp,liquid | 206.13 | J/mol×K | 372.99 | Calculated Property |
| Cp,liquid | 212.92 | J/mol×K | 398.03 | Calculated Property |
| Cp,liquid | 219.71 | J/mol×K | 423.07 | Calculated Property |
| Cp,liquid | 226.46 | J/mol×K | 448.11 | Calculated Property |
| Cp,liquid | 233.12 | J/mol×K | 473.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0017368; 0.0001680] | Pa×s | [247.98; 493.60] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.10590e+01 | |||
| Coefficient B | 1.25170e+03 | |||
| Coefficient C | -7.64380e-02 | |||
| Coefficient D | 1.25400e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 493.60 | |||
| η | 0.0017368 | Pa×s | 247.98 | Calculated Property |
| η | 0.0010635 | Pa×s | 275.27 | Calculated Property |
| η | 0.0007146 | Pa×s | 302.56 | Calculated Property |
| η | 0.0005151 | Pa×s | 329.85 | Calculated Property |
| η | 0.0003922 | Pa×s | 357.14 | Calculated Property |
| η | 0.0003119 | Pa×s | 384.44 | Calculated Property |
| η | 0.0002570 | Pa×s | 411.73 | Calculated Property |
| η | 0.0002179 | Pa×s | 439.02 | Calculated Property |
| η | 0.0001894 | Pa×s | 466.31 | Calculated Property |
| η | 0.0001680 | Pa×s | 493.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [46.36; 14.38] | kJ/mol | [247.98; 612.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 6.69790e+01 | |||
| Coefficient B | 1.25900e+00 | |||
| Coefficient C | -1.84900e+00 | |||
| Coefficient D | 1.51980e+00 | |||
| Coefficient E | -5.04550e-01 | |||
| Critical temperature, Tc (K) | 6.30300e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 612.00 | |||
| ΔvapH | 46.36 | kJ/mol | 247.98 | Calculated Property |
| ΔvapH | 44.11 | kJ/mol | 288.43 | Calculated Property |
| ΔvapH | 41.89 | kJ/mol | 328.87 | Calculated Property |
| ΔvapH | 39.61 | kJ/mol | 369.32 | Calculated Property |
| ΔvapH | 37.17 | kJ/mol | 409.77 | Calculated Property |
| ΔvapH | 34.49 | kJ/mol | 450.21 | Calculated Property |
| ΔvapH | 31.40 | kJ/mol | 490.66 | Calculated Property |
| ΔvapH | 27.66 | kJ/mol | 531.11 | Calculated Property |
| ΔvapH | 22.71 | kJ/mol | 571.55 | Calculated Property |
| ΔvapH | 14.38 | kJ/mol | 612.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [305.32; 445.43] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44465e+01 | |||
| Coefficient B | -3.60720e+03 | |||
| Coefficient C | -5.05540e+01 | |||
| Temperature range, min. | 305.32 | |||
| Temperature range, max. | 445.43 | |||
| Pvap | 1.33 | kPa | 305.32 | Calculated Property |
| Pvap | 3.01 | kPa | 320.89 | Calculated Property |
| Pvap | 6.23 | kPa | 336.46 | Calculated Property |
| Pvap | 11.95 | kPa | 352.02 | Calculated Property |
| Pvap | 21.51 | kPa | 367.59 | Calculated Property |
| Pvap | 36.64 | kPa | 383.16 | Calculated Property |
| Pvap | 59.51 | kPa | 398.73 | Calculated Property |
| Pvap | 92.72 | kPa | 414.29 | Calculated Property |
| Pvap | 139.29 | kPa | 429.86 | Calculated Property |
| Pvap | 202.65 | kPa | 445.43 | Calculated Property |
| Pvap | [0.02; 3724.92] | kPa | [247.98; 630.33] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.11744e+01 | |||
| Coefficient B | -7.84479e+03 | |||
| Coefficient C | -9.73842e+00 | |||
| Coefficient D | 5.71376e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 630.33 | |||
| Pvap | 0.02 | kPa | 247.98 | Calculated Property |
| Pvap | 0.56 | kPa | 290.46 | Calculated Property |
| Pvap | 5.40 | kPa | 332.95 | Calculated Property |
| Pvap | 28.62 | kPa | 375.43 | Calculated Property |
| Pvap | 102.20 | kPa | 417.91 | Calculated Property |
| Pvap | 278.51 | kPa | 460.40 | Calculated Property |
| Pvap | 628.42 | kPa | 502.88 | Calculated Property |
| Pvap | 1240.26 | kPa | 545.36 | Calculated Property |
| Pvap | 2224.29 | kPa | 587.85 | Calculated Property |
| Pvap | 3724.92 | kPa | 630.33 | Calculated Property |
| Pvap | [0.02; 3724.86] | kPa | [247.98; 630.37] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.33218e+01 | |||
| Coefficient B | -7.94623e+03 | |||
| Coefficient C | -1.00606e+01 | |||
| Coefficient D | 5.93974e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 630.37 | |||
| Pvap | 0.02 | kPa | 247.98 | Calculated Property |
| Pvap | 0.55 | kPa | 290.47 | Calculated Property |
| Pvap | 5.38 | kPa | 332.96 | Calculated Property |
| Pvap | 28.61 | kPa | 375.44 | Calculated Property |
| Pvap | 102.23 | kPa | 417.93 | Calculated Property |
| Pvap | 278.49 | kPa | 460.42 | Calculated Property |
| Pvap | 628.00 | kPa | 502.91 | Calculated Property |
| Pvap | 1238.99 | kPa | 545.39 | Calculated Property |
| Pvap | 2222.36 | kPa | 587.88 | Calculated Property |
| Pvap | 3724.86 | kPa | 630.37 | Calculated Property |
| Pvap | [6.35; 103.92] | kPa | [336.61; 418.52] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41132e+01 | |||
| Coefficient B | -3.40378e+03 | |||
| Coefficient C | -5.90760e+01 | |||
| Reference | Williamham, Taylor, et al., 1945 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 336.61 | |||
| Temperature range, max. | 418.52 | |||
| Pvap | 6.35 | kPa | 336.61 | Calculated Property |
| Pvap | 9.38 | kPa | 345.71 | Calculated Property |
| Pvap | 13.51 | kPa | 354.81 | Calculated Property |
| Pvap | 19.05 | kPa | 363.91 | Calculated Property |
| Pvap | 26.34 | kPa | 373.01 | Calculated Property |
| Pvap | 35.75 | kPa | 382.12 | Calculated Property |
| Pvap | 47.71 | kPa | 391.22 | Calculated Property |
| Pvap | 62.71 | kPa | 400.32 | Calculated Property |
| Pvap | 81.26 | kPa | 409.42 | Calculated Property |
| Pvap | 103.92 | kPa | 418.52 | Calculated Property |
| Pvap | [0.17; 3.39] | kPa | [273.00; 323.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.59743e+01 | |||
| Coefficient B | -4.37807e+03 | |||
| Coefficient C | -2.62680e+01 | |||
| Reference | Pitzer and Scott, 1943 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 323.00 | |||
| Pvap | 0.17 | kPa | 273.00 | Calculated Property |
| Pvap | 0.25 | kPa | 278.56 | Calculated Property |
| Pvap | 0.37 | kPa | 284.11 | Calculated Property |
| Pvap | 0.52 | kPa | 289.67 | Calculated Property |
| Pvap | 0.74 | kPa | 295.22 | Calculated Property |
| Pvap | 1.03 | kPa | 300.78 | Calculated Property |
| Pvap | 1.41 | kPa | 306.33 | Calculated Property |
| Pvap | 1.91 | kPa | 311.89 | Calculated Property |
| Pvap | 2.56 | kPa | 317.44 | Calculated Property |
| Pvap | 3.39 | kPa | 323.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [915.45; 284.11] | kg/m3 | [247.98; 630.30] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.42752e+01 | |||
| Coefficient B | 2.61430e-01 | |||
| Coefficient C | 6.30300e+02 | |||
| Coefficient D | 2.73650e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 630.30 | |||
| ρl | 915.45 | kg/m3 | 247.98 | Calculated Property |
| ρl | 882.10 | kg/m3 | 290.46 | Calculated Property |
| ρl | 846.96 | kg/m3 | 332.94 | Calculated Property |
| ρl | 809.60 | kg/m3 | 375.42 | Calculated Property |
| ρl | 769.37 | kg/m3 | 417.90 | Calculated Property |
| ρl | 725.28 | kg/m3 | 460.38 | Calculated Property |
| ρl | 675.61 | kg/m3 | 502.86 | Calculated Property |
| ρl | 616.86 | kg/m3 | 545.34 | Calculated Property |
| ρl | 539.52 | kg/m3 | 587.82 | Calculated Property |
| ρl | 284.11 | kg/m3 | 630.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 8.35e-04] | N/m | [247.98; 610.18] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -1.19420e-02 | |||
| Coefficient B | 4.92120e+01 | |||
| Coefficient C | -3.12360e+00 | |||
| Coefficient D | 5.96470e-04 | |||
| Coefficient E | -4.51520e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 610.18 | |||
| γ | 0.04 | N/m | 247.98 | Calculated Property |
| γ | 0.03 | N/m | 288.22 | Calculated Property |
| γ | 0.03 | N/m | 328.47 | Calculated Property |
| γ | 0.02 | N/m | 368.71 | Calculated Property |
| γ | 0.02 | N/m | 408.96 | Calculated Property |
| γ | 0.01 | N/m | 449.20 | Calculated Property |
| γ | 0.01 | N/m | 489.45 | Calculated Property |
| γ | 0.01 | N/m | 529.69 | Calculated Property |
| γ | 0.00 | N/m | 569.94 | Calculated Property |
| γ | 8.35e-04 | N/m | 610.18 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.01; 0.08] | W/m×K | [247.98; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 5.93870e-06 | |||
| Coefficient B | 1.35600e+00 | |||
| Coefficient C | -2.06000e+02 | |||
| Coefficient D | 6.50580e+04 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.01 | W/m×K | 247.98 | Calculated Property |
| λ | 0.02 | W/m×K | 331.54 | Calculated Property |
| λ | 0.02 | W/m×K | 415.10 | Calculated Property |
| λ | 0.03 | W/m×K | 498.65 | Calculated Property |
| λ | 0.04 | W/m×K | 582.21 | Calculated Property |
| λ | 0.05 | W/m×K | 665.77 | Calculated Property |
| λ | 0.06 | W/m×K | 749.33 | Calculated Property |
| λ | 0.06 | W/m×K | 832.88 | Calculated Property |
| λ | 0.07 | W/m×K | 916.44 | Calculated Property |
| λ | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.14; 0.10] | W/m×K | [247.98; 417.58] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | -1.87510e-02 | |||
| Coefficient B | -2.27700e+01 | |||
| Coefficient C | -1.33910e+00 | |||
| Coefficient D | -1.42810e-03 | |||
| Coefficient E | -6.16920e-07 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 417.58 | |||
| λ | 0.14 | W/m×K | 247.98 | Calculated Property |
| λ | 0.14 | W/m×K | 266.82 | Calculated Property |
| λ | 0.13 | W/m×K | 285.67 | Calculated Property |
| λ | 0.13 | W/m×K | 304.51 | Calculated Property |
| λ | 0.13 | W/m×K | 323.36 | Calculated Property |
| λ | 0.12 | W/m×K | 342.20 | Calculated Property |
| λ | 0.12 | W/m×K | 361.05 | Calculated Property |
| λ | 0.11 | W/m×K | 379.89 | Calculated Property |
| λ | 0.11 | W/m×K | 398.74 | Calculated Property |
| λ | 0.10 | W/m×K | 417.58 | Calculated Property |
Similar Compounds
Find more compounds similar to o-Xylene.
Mixtures
- Benzene, nitro- + o-Xylene
- Tetrahydropyran + o-Xylene
- Tetrahydropyran + Benzene, 1-chloro-2-methyl- + o-Xylene
- Formamide, N,N-dimethyl- + o-Xylene
- o-Xylene + 2-[2-(2-hydroxypropoxy)propoxy]-1-propanol
- Triethylene glycol + o-Xylene
- 1-Hexanol + o-Xylene
- Toluene + o-Xylene
- Benzene + o-Xylene
- 1-Butanol + o-Xylene
- Acetic acid, butyl ester + o-Xylene
- n-Hexane + o-Xylene
- Decane + o-Xylene
- Furfural + o-Xylene
- Heptane + o-Xylene + Thiophene, tetrahydro-, 1,1-dioxide
- Thiophene, tetrahydro- + o-Xylene
- Cyclohexanone + o-Xylene
- Acetic acid + o-Xylene + Water
- o-Xylene + Water
- Benzene + 2-Pyrrolidinone + o-Xylene
Find more mixtures with o-Xylene.
Sources
- KDB Vapor Pressure Data
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
- Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
- Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
- Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
- Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
- Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K
- Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
- Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
- Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
- Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
- Influence of temperature on thermodynamics of ethers + xylenes
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Phase equilibria on four binary systems containing 3-methylthiophene
- 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
- Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
- Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
- Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
- Vapor liquid equilibria and density measurement for binary mixtures of o-xylene + NMF, m-xylene +NMF and p-xylene +NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
- Isomer effect in the separation of octane and xylenes using the ionic liquid 1-ethyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}amide
- Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
- Application of [EMpy][ESO4] ionic liquid as solvent for the liquid extraction of xylenes from hexane
- Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Study of [EMim][ESO4] ionic liquid as solvent in the liquid-liquid extraction of xylenes from their mixtures with hexane
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
- Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
- Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
- 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
- Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
- Towards automated characterisation of liquid-liquid equilibria
- Prediction and measurement of phase equilibria for the extraction of BTX from naphtha reformate using BMIMPF6 ionic liquid
- 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
- Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
- 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
- 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
- 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
- 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
- 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
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- High-pressure densities of n-decane+o-xylene mixtures: Measurement and modelling
- (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
- Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
- Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
- A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
- Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
- Liquid phase behaviour of 1-hexyloxymethyl-3-methyl-imidazolium-based ionic liquids with hydrocarbons: The influence of anion
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
- Densities and volumetric properties of binary mixtures of xylene with N,N-dimethylformamide at different temperatures
- Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
- A study of densities and volumetric properties of binary mixtures of N-methyl-2-pyrrolidone with xylene at different temperatures and atmospheric pressure
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- 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
- Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- (Liquid + liquid) equilibria in the binary systems (aliphatic, or aromatic hydrocarbons + 1-ethyl-3-methylimidazolium ethylsulfate, or 1-butyl-3-methylimidazolium methylsulfate ionic liquids)
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Thermochemistry of ionic liquid-catalysed reactions. Isomerisation and transalkylation of tert-alkyl-benzenes. Are these systems ideal?
- 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
- Excess molar volumes, excess molar enthalpies, and excess isentropic compressibilities of tetrahydropyran with aromatic hydrocarbons
- 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 measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- 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
- 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
- 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
- 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
- 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
- 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
- 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 and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Phase behaviour of aqueous mixtures of acetic acid with isomers of xylene
- 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
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- 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
- Measurement and correlation of solubility of 4-chloro-2,5-dimethoxynitrobenzene and 4-chloro-2,5- dimethoxyaniline in methanol, ethanol, xylene and toluene
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- 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
- Modified solution calorimetry approach for determination of vaporization and sublimation enthalpies of branched-chain aliphatic and alkyl aromatic compounds at T = 298.15 K
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- Viscosity measurements of ortho-xylene, meta-xylene, para-xylene and ethylbenzene
- 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
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
- 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
- New aspects of relationship between the enthalpies of fusion of aromatic compounds at the melting temperatures and the enthalpies of solution in benzene at 298.15 K. Part I
- 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
- 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
- Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Molecular interactions in binary mixtures containing o-toluidine
- Excess molar volumes and excess isentropic compressibilities of 2-pyrrolidinone at 308.15K
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
- Liquid-Liquid Equilibrium for Ternary Systems Water + Acetic Acid + m-Xylene and Water + Acetic Acid + o-Xylene at (303.2 to 343.2) 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
- Solubilities of Phthalic Acid and o-Toluic Acid in Binary Acetic Acid + Water and Acetic Acid + o-Xylene Solvent Mixtures
- Mutual solubility of aromatic hydrocarbons in pyrrolidinium and ammonium-based ionic liquids and its modeling using the Cubic-Plus-Association (CPA) Equation of State
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Isobaric Vapor Liquid Equilibrium Data for the Binary Systems of Dimethyl Carbonate with Xylene Isomers at 93.13 kPa
- Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
- Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
- 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
- Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
- Volumetric Properties of the D2EHPA-o-Xylene-Neodymium (Samarium, Europium, Gadolinium, Terbium, Dysprosium) Di(2-ethylhexyl)phosphate Systems at 298.15 K
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Liquid-Liquid Equilibrium for Ternary Systems of Polyoxymethylene Dimethyl Ethers + o-Xylene + Water at 293.15 K
- Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
- Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
- 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
- Excess Molar Volumes and Surface Tensions of Xylene with 2-propanol or 2-methyl-2-propanol at 298.15 K
- Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
- 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
- Analysis and Evaluation of the Liquid-Liquid Equilibrium Data of the Extraction of Aromatics from Hydrocarbons by Tetraethylene Glycol
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
- 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
- Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
- Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
- Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
- Liquid-Liquid Equilibrium for the System Heptane + o-Xylene + Diethylene Glycol over the Temperature Range of 288.15 K to 318.15 K
- Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
- Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
- Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
- 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
- Solubilities of Benzene, Toluene, and Xylene Isomers in 1-Butyl-3-methylimidazolium Tetrafluoroborate
- Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
- Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
- Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
- Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
- 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
- Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Solubilities of 1-Hexyl-3-methylimidazole Nitrate and 1-Octyl-3-methylimidazole Nitrate in Selected Solvents
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) 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
- 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
- Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
- Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
- 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
- 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
- Liquid Liquid Equilibria for the Ternary Systems of Perfluamine + Hydrofluoroether + Benzene, Toluene, or Xylene at 298.15 K or 313.15 K
- 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
- Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- 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
- Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Molar Excess Volume of sec- and tert-Butyl Chloride with Aromatic Hydrocarbons at T = 298.15 K
- Solubilities of Vitamin K3 in Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene between (299.44 and 344.24) K
- Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
- Vapor Liquid Equilibrium of N-Formylmorpholine with Toluene and Xylene at 101.33 kPa
- Measuring Surface Tension of Liquids at High Temperature and Elevated Pressure
- 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
- Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
- Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
- Solubility of Bis(benzoxazolyl-2-methyl) Sulfide in Different Pure Solvents and Ethanol + Water Binary Mixtures between (273.25 and 325.25) K
- Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
- Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 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
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- 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
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
- 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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