- 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-Dimethylbenzene
- 1,2-Xylene
- 1,2-dimethyl-benzene ( o-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).
- 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.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| 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 | 738.15 | K | KDB |
| 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 | Thermod... |
| μ | 0.50 | debye | KDB |
| η | [0.0007680; 0.0007690] | Pa×s |
|
| η | 0.0007680 | Pa×s | Viscosi... |
| η | 0.0007690 | Pa×s | Viscosi... |
| SProt | 36.90 | J/mol×K | NIST |
| LFL | 1.10 | % in Air | KDB |
| UFL | 7.00 | % in Air | KDB |
| Tflash,cc | 297.04 | K | KDB |
| Tflash,oc | 290.37 | K | KDB |
| 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; 19.00] | kJ/mol |
|
| 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° | 36.34 | kJ/mol | Joback Calculated Property |
| 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 | Estimat... | |
| log10WS | -2.80 | Aq. Sol... | |
| logPoct/wat | 2.303 | Crippen Calculated Property | |
| McVol | 99.820 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | 3732.00 | kPa | KDB |
| 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 | 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 | |
| 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 | [417.43; 417.60] | K |
|
| Tboil | 417.60 | K | KDB |
| Tboil | 417.50 | K | Isobari... |
| Tboil | 417.43 | K | Measure... |
| Tboil | 417.55 | K | Vapor-L... |
| Tboil | 417.56 | K | Isobari... |
| Tc | 630.30 | K | KDB |
| Tfus | [247.90; 248.08] | K |
|
| Tfus | 247.90 | K | KDB |
| Tfus | 248.08 | K | Aq. Sol... |
| Ttriple | 247.80 ± 0.25 | K | NIST |
| Vc | [0.370; 0.370] | m3/kmol |
|
| Vc | 0.370 | m3/kmol | KDB |
| Vc | 0.370 | m3/kmol | NIST |
| Zc | 0.2634870 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [168.20; 192.50] | J/mol×K | [393.00; 463.00] |
|
| Cp,gas | 168.20 ± 1.70 | J/mol×K | 393.00 | NIST |
| Cp,gas | 182.00 ± 1.70 | J/mol×K | 428.00 | NIST |
| Cp,gas | 192.50 ± 2.10 | J/mol×K | 463.00 | NIST |
| Cp,liquid | [182.40; 206.70] | J/mol×K | [298.00; 347.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 180 185 190 195 200 205 300 320 340 | ||||
| Cp,liquid | 187.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 183.89 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 187.65 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 187.58 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 187.82 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 182.40 | J/mol×K | 303.00 | NIST |
| Cp,liquid | 206.70 | J/mol×K | 347.00 | NIST |
| η | [0.0004136; 0.0008710] | Pa×s | [288.15; 353.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 300 320 340 | ||||
| η | 0.0008710 | Pa×s | 288.15 | Viscosi... |
| η | 0.0008100 | Pa×s | 293.15 | Viscosi... |
| η | 0.0008092 | Pa×s | 293.15 | Viscosi... |
| η | 0.0007440 | Pa×s | 298.15 | Excess ... |
| η | 0.0007590 | Pa×s | 298.15 | Densiti... |
| η | 0.0007576 | Pa×s | 298.15 | Ultraso... |
| η | 0.0007580 | Pa×s | 298.15 | Densiti... |
| η | 0.0007560 | Pa×s | 298.15 | Viscosi... |
| η | 0.0007610 | Pa×s | 298.15 | Densiti... |
| η | 0.0006950 | Pa×s | 303.15 | Viscosi... |
| η | 0.0007172 | Pa×s | 303.15 | Viscosi... |
| η | 0.0007080 | Pa×s | 303.15 | Viscosi... |
| η | 0.0007100 | Pa×s | 303.15 | Viscome... |
| η | 0.0007095 | Pa×s | 303.15 | Densiti... |
| η | 0.0007062 | Pa×s | 303.15 | Excess ... |
| η | 0.0006950 | Pa×s | 303.15 | Thermop... |
| η | 0.0007404 | Pa×s | 303.15 | Densiti... |
| η | 0.0006900 | Pa×s | 308.15 | Densiti... |
| η | 0.0006580 | Pa×s | 308.15 | Densiti... |
| η | 0.0006690 | Pa×s | 308.15 | Ultraso... |
| η | 0.0006660 | Pa×s | 308.15 | Viscome... |
| η | 0.0006660 | Pa×s | 308.15 | Density... |
| η | 0.0006650 | Pa×s | 308.15 | Densiti... |
| η | 0.0006210 | Pa×s | 313.15 | Thermop... |
| η | 0.0006210 | Pa×s | 313.15 | Viscosi... |
| η | 0.0006292 | Pa×s | 313.15 | Viscosi... |
| η | 0.0006261 | Pa×s | 313.15 | Densiti... |
| η | 0.0006451 | Pa×s | 313.15 | Densiti... |
| η | 0.0006280 | Pa×s | 313.15 | Viscome... |
| η | 0.0005972 | Pa×s | 318.15 | Ultraso... |
| η | 0.0005910 | Pa×s | 318.15 | Viscome... |
| η | 0.0006117 | Pa×s | 318.15 | Densiti... |
| η | 0.0005890 | Pa×s | 318.15 | Densiti... |
| η | 0.0005910 | Pa×s | 318.15 | Density... |
| η | 0.0005554 | Pa×s | 323.15 | Excess ... |
| η | 0.0005600 | Pa×s | 323.15 | Viscome... |
| η | 0.0005584 | Pa×s | 323.15 | Densiti... |
| η | 0.0005711 | Pa×s | 323.15 | Densiti... |
| η | 0.0005433 | Pa×s | 328.15 | Densiti... |
| η | 0.0005105 | Pa×s | 333.15 | Densiti... |
| η | 0.0005020 | Pa×s | 333.15 | Densiti... |
| η | 0.0004544 | Pa×s | 343.15 | Densiti... |
| η | 0.0004136 | Pa×s | 353.15 | Densiti... |
| ΔfusH | [13.60; 13.60] | kJ/mol | [247.80; 247.82] |
|
| ΔfusH | 13.60 | kJ/mol | 247.80 | NIST |
| ΔfusH | 13.60 | kJ/mol | 247.80 | NIST |
| ΔfusH | 13.60 | kJ/mol | 247.82 | NIST |
| ΔsubH | 60.10 | kJ/mol | 248.00 | NIST |
| ΔvapH | [36.24; 45.00] | kJ/mol | [298.00; 598.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 300 400 500 600 | ||||
| ΔvapH | 43.07 | kJ/mol | 298.00 | Enthalp... |
| ΔvapH | 45.00 | kJ/mol | 298.00 | NIST |
| ΔvapH | 41.10 | kJ/mol | 376.00 | NIST |
| ΔvapH | 40.80 | kJ/mol | 378.00 | NIST |
| ΔvapH | 39.80 | kJ/mol | 401.00 | NIST |
| ΔvapH | 36.82 | kJ/mol | 417.50 | KDB |
| ΔvapH | 36.24 | kJ/mol | 417.60 | NIST |
| ΔvapH | 38.00 | kJ/mol | 444.50 | NIST |
| ΔvapH | 36.70 | kJ/mol | 521.00 | NIST |
| ΔvapH | 36.70 | kJ/mol | 598.50 | NIST |
| Pvap | [0.88; 250.00] | kPa | [298.15; 456.10] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 400 450 | ||||
| Pvap | 0.88 | kPa | 298.15 | (Vapour... |
| Pvap | 2.05 | kPa | 313.15 | Vapor-l... |
| Pvap | 3.60 | kPa | 323.15 | Vapor-L... |
| Pvap | 3.46 | kPa | 323.15 | Vapor-l... |
| Pvap | 5.44 | kPa | 333.15 | Vapor l... |
| Pvap | 5.32 | kPa | 333.15 | Vapor l... |
| Pvap | 5.61 | kPa | 333.15 | Vapor-l... |
| Pvap | 5.45 | kPa | 333.15 | Vapor l... |
| Pvap | 8.54 | kPa | 343.15 | Vapor-l... |
| Pvap | 8.47 | kPa | 343.15 | Vapor l... |
| Pvap | 9.18 | kPa | 345.15 | Vapour-... |
| Pvap | 11.27 | kPa | 350.15 | Vapour-... |
| Pvap | 12.66 | kPa | 353.15 | Vapor l... |
| Pvap | 12.73 | kPa | 353.15 | Vapor-l... |
| Pvap | 12.80 | kPa | 353.15 | Vapor l... |
| Pvap | 12.71 | kPa | 353.15 | Vapor l... |
| Pvap | 13.73 | kPa | 355.15 | Vapour-... |
| Pvap | 14.75 | kPa | 357.30 | Extensi... |
| Pvap | 16.62 | kPa | 360.15 | Vapour-... |
| Pvap | 18.65 | kPa | 363.15 | Vapor-l... |
| Pvap | 20.00 | kPa | 365.15 | Vapour-... |
| Pvap | 20.40 | kPa | 365.49 | Vapor l... |
| Pvap | 26.73 | kPa | 373.15 | Vapor-l... |
| Pvap | 29.61 | kPa | 376.70 | Extensi... |
| Pvap | 30.14 | kPa | 376.75 | Vapor l... |
| Pvap | 31.66 | kPa | 378.15 | Vapor-l... |
| Pvap | 37.35 | kPa | 383.15 | Vapor-l... |
| Pvap | 40.20 | kPa | 385.55 | Vapor l... |
| Pvap | 43.63 | kPa | 388.15 | Vapor-l... |
| Pvap | 49.44 | kPa | 392.70 | Extensi... |
| Pvap | 50.43 | kPa | 392.87 | Vapor l... |
| Pvap | 50.60 | kPa | 393.04 | Vapor-L... |
| Pvap | 51.01 | kPa | 393.15 | Vapor-l... |
| Pvap | 60.03 | kPa | 398.66 | Vapor l... |
| Pvap | 64.27 | kPa | 401.50 | Extensi... |
| Pvap | 68.42 | kPa | 403.15 | Vapor-l... |
| Pvap | 70.27 | kPa | 404.09 | Vapor l... |
| Pvap | 80.41 | kPa | 408.83 | Vapor l... |
| Pvap | 90.54 | kPa | 413.06 | Vapor l... |
| Pvap | 90.18 | kPa | 413.15 | Vapor-l... |
| Pvap | 90.39 | kPa | 413.15 | Vapor-L... |
| Pvap | 93.13 | kPa | 414.41 | Refract... |
| Pvap | 101.85 | kPa | 417.28 | Vapor l... |
| Pvap | 101.30 | kPa | 417.43 | Measure... |
| Pvap | 102.78 | kPa | 418.60 | Extensi... |
| Pvap | 250.00 | kPa | 456.10 | Isobari... |
| n0 | [1.48580; 1.50830] | [288.15; 318.15] |
|
|
|
T(K) Refractive Index 1.49 1.49 1.5 1.5 1.51 1.51 290 300 310 | ||||
| n0 | 1.50830 | 288.15 | Densiti... | |
| n0 | 1.50720 | 288.15 | Excess ... | |
| n0 | 1.50830 | 288.15 | Refract... | |
| n0 | 1.50570 | 293.10 | Volumet... | |
| n0 | 1.48580 | 293.15 | Activit... | |
| n0 | 1.50150 | 293.15 | Volumet... | |
| n0 | 1.50550 | 293.15 | Excess ... | |
| n0 | 1.50550 | 293.15 | Bubble ... | |
| n0 | 1.50570 | 293.15 | Densiti... | |
| n0 | 1.50573 | 293.15 | A study... | |
| n0 | 1.50550 | 293.15 | Refract... | |
| n0 | 1.50470 | 293.15 | Excess ... | |
| n0 | 1.50550 | 293.15 | Solubil... | |
| n0 | 1.50550 | 293.15 | Densiti... | |
| n0 | 1.50260 | 298.00 | Vapor-L... | |
| n0 | 1.50180 | 298.15 | Excess ... | |
| n0 | 1.50280 | 298.15 | Phase e... | |
| n0 | 1.50280 | 298.15 | Phase e... | |
| n0 | 1.50180 | 298.15 | Liquid-... | |
| n0 | 1.50200 | 298.15 | Isobari... | |
| n0 | 1.50260 | 298.15 | Vapor-L... | |
| n0 | 1.50570 | 298.15 | A study... | |
| n0 | 1.50240 | 298.15 | Densiti... | |
| n0 | 1.50262 | 298.15 | Density... | |
| n0 | 1.50300 | 298.15 | Bubble ... | |
| n0 | 1.50290 | 298.15 | Refract... | |
| n0 | 1.50290 | 298.15 | Densiti... | |
| n0 | 1.50570 | 298.15 | Densiti... | |
| n0 | 1.50295 | 298.15 | KDB | |
| n0 | 1.50000 | 303.15 | Excess ... | |
| n0 | 1.50020 | 303.15 | Refract... | |
| n0 | 1.50020 | 303.15 | Densiti... | |
| n0 | 1.49750 | 308.15 | Densiti... | |
| n0 | 1.49750 | 308.15 | Refract... | |
| n0 | 1.50310 | 308.15 | Topolog... | |
| n0 | 1.49480 | 313.15 | Densiti... | |
| n0 | 1.49480 | 313.15 | Refract... | |
| n0 | 1.49466 | 313.15 | Density... | |
| n0 | 1.49210 | 318.15 | Refract... | |
| n0 | 1.49210 | 318.15 | Densiti... | |
| ρl | [746.76; 884.09] | kg/m3 | [288.15; 353.15] |
|
|
T(K) Liquid Density (kg/m3) 740 760 780 800 820 840 860 880 300 320 340 | ||||
| ρl | 883.91 | kg/m3 | 288.15 | Thermod... |
| ρl | 884.09 | kg/m3 | 288.15 | Densiti... |
| ρl | 884.07 | kg/m3 | 288.15 | Effect ... |
| ρl | 880.00 | kg/m3 | 293.00 | KDB |
| ρl | 879.68 | kg/m3 | 293.15 | Isobari... |
| ρl | 879.72 | kg/m3 | 293.15 | Thermod... |
| ρl | 879.83 | kg/m3 | 293.15 | Densiti... |
| ρl | 878.60 | kg/m3 | 293.15 | Excess ... |
| ρl | 875.36 | kg/m3 | 298.15 | Acousti... |
| ρl | 875.81 | kg/m3 | 298.15 | Vapor L... |
| ρl | 875.90 | kg/m3 | 298.15 | Bubble ... |
| ρl | 859.54 | kg/m3 | 298.15 | Isobari... |
| ρl | 859.54 | kg/m3 | 298.15 | Isobari... |
| ρl | 875.50 | kg/m3 | 298.15 | Isobari... |
| ρl | 875.52 | kg/m3 | 298.15 | Evaluat... |
| ρl | 875.91 | kg/m3 | 298.15 | Thermod... |
| ρl | 875.72 | kg/m3 | 298.15 | Excess ... |
| ρl | 875.99 | kg/m3 | 298.15 | Molar E... |
| ρl | 875.92 | kg/m3 | 298.15 | Excess ... |
| ρl | 875.92 | kg/m3 | 298.15 | Excess ... |
| ρl | 875.00 | kg/m3 | 298.15 | Excess ... |
| ρl | 875.00 | kg/m3 | 298.15 | Excess ... |
| ρl | 875.60 | kg/m3 | 298.15 | Volumet... |
| ρl | 875.81 | kg/m3 | 298.15 | Isobari... |
| ρl | 875.57 | kg/m3 | 298.15 | Densiti... |
| ρl | 875.51 | kg/m3 | 298.15 | Thermod... |
| ρl | 875.99 | kg/m3 | 298.15 | Thermod... |
| ρl | 874.89 | kg/m3 | 298.15 | Experim... |
| ρl | 875.67 | kg/m3 | 298.15 | Effect ... |
| ρl | 875.91 | kg/m3 | 298.15 | Heat ca... |
| ρl | 875.90 | kg/m3 | 298.15 | Molar E... |
| ρl | 875.50 | kg/m3 | 298.20 | Isobari... |
| ρl | 871.70 | kg/m3 | 303.15 | Heat ca... |
| ρl | 871.30 | kg/m3 | 303.15 | Thermod... |
| ρl | 872.25 | kg/m3 | 303.15 | Excess ... |
| ρl | 871.70 | kg/m3 | 303.15 | Thermod... |
| ρl | 871.31 | kg/m3 | 303.15 | Densiti... |
| ρl | 871.50 | kg/m3 | 303.15 | Densiti... |
| ρl | 867.48 | kg/m3 | 308.15 | Thermod... |
| ρl | 867.05 | kg/m3 | 308.15 | Densiti... |
| ρl | 867.30 | kg/m3 | 308.15 | Effect ... |
| ρl | 867.48 | kg/m3 | 308.15 | Heat ca... |
| ρl | 867.07 | kg/m3 | 308.15 | Thermod... |
| ρl | 867.20 | kg/m3 | 308.15 | Densiti... |
| ρl | 866.51 | kg/m3 | 308.15 | Acousti... |
| ρl | 862.79 | kg/m3 | 313.15 | Densiti... |
| ρl | 862.80 | kg/m3 | 313.15 | Densiti... |
| ρl | 862.83 | kg/m3 | 313.15 | Thermod... |
| ρl | 859.67 | kg/m3 | 313.15 | Excess ... |
| ρl | 858.81 | kg/m3 | 318.15 | Effect ... |
| ρl | 858.57 | kg/m3 | 318.15 | Thermod... |
| ρl | 858.53 | kg/m3 | 318.15 | Densiti... |
| ρl | 858.80 | kg/m3 | 318.15 | Densiti... |
| ρl | 840.84 | kg/m3 | 323.15 | Excess ... |
| ρl | 854.30 | kg/m3 | 323.15 | Thermod... |
| ρl | 854.30 | kg/m3 | 323.15 | Densiti... |
| ρl | 850.24 | kg/m3 | 328.15 | Effect ... |
| ρl | 850.01 | kg/m3 | 328.15 | Thermod... |
| ρl | 845.71 | kg/m3 | 333.15 | Thermod... |
| ρl | 815.74 | kg/m3 | 333.15 | Excess ... |
| ρl | 784.38 | kg/m3 | 343.15 | Excess ... |
| ρl | 746.76 | kg/m3 | 353.15 | Excess ... |
| ΔfusS | 54.87 | J/mol×K | 247.82 | NIST |
| csound,fluid | [1240.87; 1381.29] | m/s | [288.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1240 1260 1280 1300 1320 1340 1360 1380 290 300 310 320 | ||||
| csound,fluid | 1381.29 | m/s | 288.15 | Influen... |
| csound,fluid | 1371.75 | m/s | 290.65 | Influen... |
| csound,fluid | 1362.16 | m/s | 293.15 | Influen... |
| csound,fluid | 1369.00 | m/s | 293.15 | Densiti... |
| csound,fluid | 1367.70 | m/s | 293.15 | Physico... |
| csound,fluid | 1351.83 | m/s | 295.65 | Influen... |
| csound,fluid | 1347.50 | m/s | 298.15 | Physico... |
| csound,fluid | 1341.51 | m/s | 298.15 | Influen... |
| csound,fluid | 1346.00 | m/s | 298.15 | Isentro... |
| csound,fluid | 1331.21 | m/s | 300.65 | Influen... |
| csound,fluid | 1320.96 | m/s | 303.15 | Influen... |
| csound,fluid | 1329.40 | m/s | 303.15 | Physico... |
| csound,fluid | 1328.00 | m/s | 303.15 | Densiti... |
| csound,fluid | 1310.79 | m/s | 305.65 | Influen... |
| csound,fluid | 1300.66 | m/s | 308.15 | Influen... |
| csound,fluid | 1313.30 | m/s | 308.15 | Physico... |
| csound,fluid | 1290.59 | m/s | 310.65 | Influen... |
| csound,fluid | 1298.50 | m/s | 313.15 | Physico... |
| csound,fluid | 1280.61 | m/s | 313.15 | Influen... |
| csound,fluid | 1289.00 | m/s | 313.15 | Densiti... |
| csound,fluid | 1270.55 | m/s | 315.65 | Influen... |
| csound,fluid | 1285.20 | m/s | 318.15 | Physico... |
| csound,fluid | 1260.62 | m/s | 318.15 | Influen... |
| csound,fluid | 1250.66 | m/s | 320.65 | Influen... |
| csound,fluid | 1240.87 | m/s | 323.15 | Influen... |
| γ | [0.02; 0.03] | N/m | [293.20; 343.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 0.03 0.03 300 320 340 | ||||
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 298.15 | Densiti... |
| γ | 0.03 | N/m | 298.15 | Excess ... |
| γ | 0.03 | N/m | 298.15 | Experim... |
| γ | 0.03 | N/m | 303.15 | Excess ... |
| γ | 0.03 | N/m | 303.15 | Surface... |
| γ | 0.03 | N/m | 303.15 | Densiti... |
| γ | 0.03 | N/m | 308.15 | Excess ... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 308.15 | Densiti... |
| γ | 0.03 | N/m | 313.15 | Surface... |
| γ | 0.03 | N/m | 318.15 | Surface... |
| γ | 0.03 | N/m | 323.15 | Surface... |
| γ | 0.03 | N/m | 333.15 | Surface... |
| γ | 0.02 | N/m | 343.15 | Surface... |
| λ | [0.12; 0.14] | W/m×K | [257.75; 329.09] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.13 0.13 0.14 260 280 300 320 | ||||
| λ | 0.14 | W/m×K | 257.75 | Thermal... |
| λ | 0.14 | W/m×K | 257.96 | Thermal... |
| λ | 0.14 | W/m×K | 258.10 | Thermal... |
| λ | 0.13 | W/m×K | 277.07 | Thermal... |
| λ | 0.13 | W/m×K | 277.27 | Thermal... |
| λ | 0.13 | W/m×K | 277.42 | Thermal... |
| λ | 0.13 | W/m×K | 295.56 | Thermal... |
| λ | 0.13 | W/m×K | 295.78 | Thermal... |
| λ | 0.13 | W/m×K | 295.91 | Thermal... |
| λ | 0.13 | W/m×K | 312.07 | Thermal... |
| λ | 0.13 | W/m×K | 312.29 | Thermal... |
| λ | 0.13 | W/m×K | 312.44 | Thermal... |
| λ | 0.12 | W/m×K | 328.72 | Thermal... |
| λ | 0.12 | W/m×K | 328.94 | Thermal... |
| λ | 0.12 | W/m×K | 329.09 | Thermal... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [305.32; 445.43] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
| 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; 3724.86] | kPa | [247.98; 630.37] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.33218e+01 | |||
| Coefficient B | -7.94623e+03 | |||
| Coefficient C | -1.00606e+01 | |||
| Coefficient D | 5.93974e-06 | |||
| Temperature range, min. | 247.98 | |||
| Temperature range, max. | 630.37 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
| 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 |
Similar Compounds
Find more compounds similar to o-Xylene.
Mixtures
- n-Hexane + o-Xylene
- Toluene + 2-Pyrrolidinone + o-Xylene
- 2-Propenoic acid, butyl ester + o-Xylene
- Benzene + Tetrahydropyran + o-Xylene
- Toluene + Tetrahydropyran + o-Xylene
- Decane + o-Xylene
- Propanoic acid, propyl ester + o-Xylene
- Acetic acid, butyl ester + o-Xylene
- Phenol, 2-methyl- + o-Xylene
- o-Xylene + Tetrahydrofuran
- Formamide, N,N-dimethyl- + o-Xylene
- Propane, 2-methoxy-2-methyl- + o-Xylene
- Propane, 2-ethoxy-2-methyl- + o-Xylene
- Toluene + o-Xylene
- o-Xylene + Thiophene, tetrahydro-, 1,1-dioxide
- Thiophene, tetrahydro- + o-Xylene
- Formamide, N-methyl- + o-Xylene
- Thiophene, 3-methyl- + o-Xylene
- 1-Hexanol + o-Xylene
- Octane + o-Xylene
Find more mixtures with o-Xylene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- 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
- 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
- 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
- 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
- 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
- Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
- 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
- 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
- The Yaws Handbook of Vapor Pressure
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