- InChI
- InChI=1S/C7H14/c1-7-5-3-2-4-6-7/h7H,2-6H2,1H3
- InChI Key
- UAEPNZWRGJTJPN-UHFFFAOYSA-N
- Formula
- C7H14
- SMILES
- CC1CCCCC1
- Molecular Weight1
- 98.19
- CAS
- 108-87-2
- Other Names
-
- Cyclohexylmethane
- Hexahydroxytoluene
- Metylocykloheksan
- NSC 9391
- Sextone B
- Toluene hexahydride
- Toluene, hexahydro-
- UN 2296
- hexahydrotoluene
- methylcyclohexane
- ω : Acentric Factor.
- AP : Aniline Point (K).
- 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).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2333; 0.2477] |
|
|
| ω | 0.2477 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2333 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.2350 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2360 | KDB | |
| AP | 314.150 | K | KDB |
| ΔcH°liquid | [-4604.90; -4564.30] | kJ/mol |
|
| ΔcH°liquid | -4565.29 ± 0.96 | kJ/mol | NIST |
| ΔcH°liquid | -4564.30 ± 1.90 | kJ/mol | NIST |
| ΔcH°liquid | -4604.90 | kJ/mol | NIST |
| μ | [0.00; 0.00] | debye |
|
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 0.00 | debye | KDB |
| η | 0.0006830 | Pa×s | Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K |
| ΔfG° | [27.30; 27.33] | kJ/mol |
|
| ΔfG° | 27.33 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 27.30 | kJ/mol | KDB |
| Rg | 3.7470 | KDB | |
| Δc,grossH | 4565.29 | kJ/mol | KDB |
| Δc,netH | 4257.136 | kJ/mol | KDB |
| ΔfH°gas | [-159.90; -154.80] | kJ/mol |
|
| ΔfH°gas | -154.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -154.90 | kJ/mol | KDB |
| ΔfH°gas | -154.80 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | -159.90 | kJ/mol | NIST |
| ΔfH°liquid | [-195.30; -190.20] | kJ/mol |
|
| ΔfH°liquid | -190.20 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -195.30 ± 1.90 | kJ/mol | NIST |
| ΔfusH° | 5.72 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [31.60; 35.44] | kJ/mol |
|
| ΔvapH° | 35.44 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 35.40 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 35.40 | kJ/mol | NIST |
| ΔvapH° | 35.30 | kJ/mol | NIST |
| ΔvapH° | 35.20 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 35.20 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 35.35 | kJ/mol | NIST |
| ΔvapH° | 35.40 | kJ/mol | NIST |
| ΔvapH° | Outlier 31.60 | kJ/mol | NIST |
| IE | [9.62; 9.85] | eV |
|
| IE | 9.64 ± 0.10 | eV | NIST |
| IE | 9.62 ± 0.05 | eV | NIST |
| IE | 9.64 | eV | NIST |
| IE | 9.64 ± 0.10 | eV | NIST |
| IE | 9.69 ± 0.15 | eV | NIST |
| IE | 9.76 ± 0.03 | eV | NIST |
| IE | Outlier 9.85 ± 0.03 | eV | NIST |
| log10WS | [-3.85; -3.85] |
|
|
| log10WS | -3.85 | Aq. Solubility Prediction | |
| log10WS | -3.85 | Estimated Solubility | |
| logPoct/wat | 2.587 | Crippen Calculated Property | |
| McVol | 98.630 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [3470.00; 3480.00] | kPa |
|
| Pc | 3470.00 | kPa | Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method |
| Pc | 3480.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Pc | 3479.50 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3471.51 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 3471.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3480.00 | kPa | KDB |
| Pc | 3480.00 ± 20.00 | kPa | NIST |
| Pc | 3471.00 ± 30.40 | kPa | NIST |
| Pc | 3477.68 ± 5.06 | kPa | NIST |
| Ptriple | 1.52e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | [266.08; 266.97] | kg/m3 |
|
| ρc | 266.08 ± 1.96 | kg/m3 | NIST |
| ρc | 266.97 ± 2.95 | kg/m3 | NIST |
| ρc | 266.58 ± 2.95 | kg/m3 | NIST |
| ρc | 266.08 ± 1.96 | kg/m3 | NIST |
| Inp | [709.00; 760.00] |
|
|
| Inp | 717.10 | NIST | |
| Inp | 722.20 | NIST | |
| Inp | Outlier 758.30 | NIST | |
| Inp | 737.00 | NIST | |
| Inp | Outlier 754.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 733.10 | NIST | |
| Inp | Outlier 750.40 | NIST | |
| Inp | Outlier 759.70 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 724.10 | NIST | |
| Inp | 724.20 | NIST | |
| Inp | 724.40 | NIST | |
| Inp | 723.20 | NIST | |
| Inp | Outlier 757.20 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 740.00 | NIST | |
| Inp | 726.10 | NIST | |
| Inp | 730.20 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 721.40 | NIST | |
| Inp | 723.80 | NIST | |
| Inp | 726.20 | NIST | |
| Inp | 734.60 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 722.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 723.10 | NIST | |
| Inp | 725.40 | NIST | |
| Inp | 727.90 | NIST | |
| Inp | 730.60 | NIST | |
| Inp | 733.30 | NIST | |
| Inp | 736.30 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 724.40 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 744.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 730.90 | NIST | |
| Inp | 731.90 | NIST | |
| Inp | Outlier 754.00 | NIST | |
| Inp | 737.00 | NIST | |
| Inp | 725.80 | NIST | |
| Inp | 731.50 | NIST | |
| Inp | 725.80 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 735.40 | NIST | |
| Inp | 735.70 | NIST | |
| Inp | 730.10 | NIST | |
| Inp | 730.90 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 728.30 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 732.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 741.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | Outlier 751.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 726.60 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | Outlier 754.00 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 731.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 733.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | Outlier 760.00 | NIST | |
| Inp | 738.00 | NIST | |
| Inp | 713.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 739.00 | NIST | |
| Inp | 717.70 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | 720.20 | NIST | |
| Inp | 715.27 | NIST | |
| Inp | 715.65 | NIST | |
| Inp | 718.30 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 720.30 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 723.10 | NIST | |
| Inp | 719.40 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 718.30 | NIST | |
| Inp | 720.00 | NIST | |
| Inp | 720.30 | NIST | |
| Inp | 716.67 | NIST | |
| Inp | 716.41 | NIST | |
| Inp | 716.54 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 721.90 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 716.90 | NIST | |
| Inp | 710.40 | NIST | |
| Inp | 713.04 | NIST | |
| Inp | 714.82 | NIST | |
| Inp | 715.22 | NIST | |
| Inp | 718.06 | NIST | |
| Inp | 719.89 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 723.05 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 728.00 | NIST | |
| Inp | 719.70 | NIST | |
| Inp | 715.75 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 723.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 718.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 716.10 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 730.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | Outlier 755.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 746.00 | NIST | |
| Inp | Outlier 748.00 | NIST | |
| Inp | Outlier 750.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 724.00 | NIST | |
| Inp | 734.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 726.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 709.00 | NIST | |
| Inp | 729.00 | NIST | |
| Inp | Outlier 748.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 725.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 736.00 | NIST | |
| Inp | Outlier 750.00 | NIST | |
| Inp | 716.00 | NIST | |
| Inp | 737.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 717.70 | NIST | |
| Inp | 721.00 | NIST | |
| Inp | 719.00 | NIST | |
| Inp | Outlier 750.00 | NIST | |
| Inp | 717.00 | NIST | |
| Inp | 714.00 | NIST | |
| Inp | 727.00 | NIST | |
| Inp | 735.00 | NIST | |
| Inp | 715.00 | NIST | |
| Inp | 715.75 | NIST | |
| Inp | 718.00 | NIST | |
| Ip | [756.00; 814.00] |
|
|
| Ip | 814.00 | NIST | |
| Ip | 794.00 | NIST | |
| Ip | 799.00 | NIST | |
| Ip | 804.00 | NIST | |
| Ip | 790.00 | NIST | |
| Ip | 814.00 | NIST | |
| Ip | 788.00 | NIST | |
| Ip | 800.00 | NIST | |
| Ip | 778.00 | NIST | |
| Ip | 780.00 | NIST | |
| Ip | 766.00 | NIST | |
| Ip | 756.00 | NIST | |
| Ip | 778.00 | NIST | |
| Ip | 785.00 | NIST | |
| Ip | 759.00 | NIST | |
| Ip | 759.00 | NIST | |
| Ip | 762.00 | NIST | |
| Ip | 762.00 | NIST | |
| Ip | 776.00 | NIST | |
| Ip | 776.00 | NIST | |
| Ip | 757.00 | NIST | |
| Ip | 800.00 | NIST | |
| Ip | 760.00 | NIST | |
| Ip | 784.00 | NIST | |
| Ip | 780.00 | NIST | |
| Ip | 781.00 | NIST | |
| Ip | 776.00 | NIST | |
| Ip | 766.00 | NIST | |
| Ip | 759.00 | NIST | |
| Ip | 760.00 | NIST | |
| Ip | 814.00 | NIST | |
| S°gas | 343.30 | J/mol×K | NIST |
| S°liquid | [247.90; 248.10] | J/mol×K |
|
| S°liquid | 247.90 | J/mol×K | NIST |
| S°liquid | 248.10 | J/mol×K | NIST |
| Tboil | [353.05; 379.40] | K |
|
| Tboil | 373.96 | K | Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa |
| Tboil | 372.13 | K | Measurement on vapor pressure, density and viscosity for binary mixtures of JP-10 and methylcyclohexane |
| Tboil | 373.88 | K | Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa |
| Tboil | 374.07 | K | VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa |
| Tboil | 373.90 | K | Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K |
| Tboil | 374.08 | K | Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere |
| Tboil | 373.35 | K | Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of 3,3-Dimethyloxetane + Methyl Cyclohexane and 3-Chloro-2,2-dimethyl-1-propanol + Methyl Cyclohexane at 101.3 kPa |
| Tboil | 373.96 | K | Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene |
| Tboil | 374.09 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 374.08 | K | KDB |
| Tboil | 374.06 ± 0.20 | K | NIST |
| Tboil | 374.12 ± 0.20 | K | NIST |
| Tboil | 373.80 ± 0.30 | K | NIST |
| Tboil | 374.10 | K | NIST |
| Tboil | 373.00 ± 2.00 | K | NIST |
| Tboil | 373.50 ± 1.00 | K | NIST |
| Tboil | 374.10 | K | NIST |
| Tboil | 374.07 ± 0.10 | K | NIST |
| Tboil | 374.07 ± 0.20 | K | NIST |
| Tboil | 374.20 ± 1.50 | K | NIST |
| Tboil | 374.00 ± 2.00 | K | NIST |
| Tboil | 373.90 ± 0.30 | K | NIST |
| Tboil | 374.08 ± 0.15 | K | NIST |
| Tboil | 376.00 ± 2.00 | K | NIST |
| Tboil | 374.10 ± 0.60 | K | NIST |
| Tboil | 374.00 ± 2.00 | K | NIST |
| Tboil | 374.00 ± 1.00 | K | NIST |
| Tboil | 373.91 ± 0.30 | K | NIST |
| Tboil | 373.70 ± 1.00 | K | NIST |
| Tboil | 373.50 ± 2.00 | K | NIST |
| Tboil | 374.10 ± 1.50 | K | NIST |
| Tboil | 374.00 ± 2.00 | K | NIST |
| Tboil | 374.00 ± 0.40 | K | NIST |
| Tboil | 374.00 ± 0.30 | K | NIST |
| Tboil | 374.00 ± 2.00 | K | NIST |
| Tboil | 373.00 ± 5.00 | K | NIST |
| Tboil | 373.80 ± 1.00 | K | NIST |
| Tboil | 374.00 ± 3.00 | K | NIST |
| Tboil | 373.70 ± 1.50 | K | NIST |
| Tboil | 374.07 ± 0.20 | K | NIST |
| Tboil | 373.80 ± 1.00 | K | NIST |
| Tboil | 373.80 ± 1.00 | K | NIST |
| Tboil | 373.20 ± 0.60 | K | NIST |
| Tboil | 374.10 ± 1.00 | K | NIST |
| Tboil | 374.10 ± 1.00 | K | NIST |
| Tboil | 374.08 ± 0.20 | K | NIST |
| Tboil | 373.50 ± 1.50 | K | NIST |
| Tboil | 374.00 ± 0.30 | K | NIST |
| Tboil | 375.00 ± 2.00 | K | NIST |
| Tboil | 373.00 ± 0.00 | K | NIST |
| Tboil | 373.00 ± 2.00 | K | NIST |
| Tboil | 373.50 ± 1.50 | K | NIST |
| Tboil | 374.13 ± 0.50 | K | NIST |
| Tboil | 374.09 ± 0.20 | K | NIST |
| Tboil | 374.10 ± 0.20 | K | NIST |
| Tboil | 374.10 ± 0.30 | K | NIST |
| Tboil | 373.20 ± 2.00 | K | NIST |
| Tboil | 374.05 ± 0.50 | K | NIST |
| Tboil | 373.75 ± 0.50 | K | NIST |
| Tboil | 374.00 ± 0.40 | K | NIST |
| Tboil | 374.40 ± 1.00 | K | NIST |
| Tboil | 374.20 ± 0.15 | K | NIST |
| Tboil | 374.20 ± 0.30 | K | NIST |
| Tboil | 374.02 ± 0.22 | K | NIST |
| Tboil | 374.40 ± 0.50 | K | NIST |
| Tboil | 373.15 ± 1.00 | K | NIST |
| Tboil | 373.95 ± 0.30 | K | NIST |
| Tboil | 374.09 ± 0.05 | K | NIST |
| Tboil | 374.05 ± 0.30 | K | NIST |
| Tboil | 373.95 ± 0.50 | K | NIST |
| Tboil | 374.08 ± 0.01 | K | NIST |
| Tboil | 374.09 ± 0.20 | K | NIST |
| Tboil | 374.20 ± 0.20 | K | NIST |
| Tboil | 373.80 ± 0.40 | K | NIST |
| Tboil | Outlier 353.05 ± 0.30 | K | NIST |
| Tboil | 374.08 ± 0.06 | K | NIST |
| Tboil | 374.30 ± 0.20 | K | NIST |
| Tboil | 374.05 ± 0.50 | K | NIST |
| Tboil | 374.09 ± 0.10 | K | NIST |
| Tboil | 374.02 ± 0.20 | K | NIST |
| Tboil | 374.32 ± 0.15 | K | NIST |
| Tboil | 373.60 ± 0.40 | K | NIST |
| Tboil | 373.95 ± 0.20 | K | NIST |
| Tboil | 374.20 ± 0.60 | K | NIST |
| Tboil | 374.15 ± 0.50 | K | NIST |
| Tboil | 373.95 ± 0.20 | K | NIST |
| Tboil | 373.00 ± 3.00 | K | NIST |
| Tboil | 373.95 ± 0.50 | K | NIST |
| Tboil | 372.95 ± 2.50 | K | NIST |
| Tboil | 373.95 ± 0.30 | K | NIST |
| Tboil | 373.95 ± 0.30 | K | NIST |
| Tboil | 374.00 ± 0.60 | K | NIST |
| Tboil | 375.15 ± 1.50 | K | NIST |
| Tboil | 374.15 ± 1.50 | K | NIST |
| Tboil | 374.30 ± 0.30 | K | NIST |
| Tboil | 374.30 ± 0.50 | K | NIST |
| Tboil | 374.10 ± 0.30 | K | NIST |
| Tboil | 373.95 ± 0.50 | K | NIST |
| Tboil | 374.35 ± 0.30 | K | NIST |
| Tboil | 374.40 ± 0.30 | K | NIST |
| Tboil | 373.85 ± 0.30 | K | NIST |
| Tboil | 373.90 ± 0.20 | K | NIST |
| Tboil | 374.40 ± 1.00 | K | NIST |
| Tboil | 373.45 ± 0.15 | K | NIST |
| Tboil | 373.60 ± 1.00 | K | NIST |
| Tboil | 373.60 ± 0.60 | K | NIST |
| Tboil | 376.00 ± 2.00 | K | NIST |
| Tboil | Outlier 379.40 ± 5.00 | K | NIST |
| Tboil | 374.00 ± 5.00 | K | NIST |
| Tboil | 375.00 ± 3.00 | K | NIST |
| Tboil | 375.00 ± 3.00 | K | NIST |
| Tboil | 373.30 ± 1.50 | K | NIST |
| Tboil | 374.00 ± 3.00 | K | NIST |
| Tboil | 376.00 ± 5.00 | K | NIST |
| Tboil | 374.00 ± 5.00 | K | NIST |
| Tboil | 375.00 ± 5.00 | K | NIST |
| Tc | [572.10; 574.70] | K |
|
| Tc | 572.10 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Tc | 572.10 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 572.19 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 572.19 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 572.10 | K | KDB |
| Tc | 572.10 ± 0.20 | K | NIST |
| Tc | 572.10 | K | NIST |
| Tc | 572.20 ± 0.57 | K | NIST |
| Tc | 572.12 ± 0.20 | K | NIST |
| Tc | 572.12 ± 0.20 | K | NIST |
| Tc | 573.20 ± 2.00 | K | NIST |
| Tc | 572.70 ± 0.60 | K | NIST |
| Tc | 572.28 ± 0.05 | K | NIST |
| Tc | Outlier 574.70 ± 2.00 | K | NIST |
| Tfus | [144.00; 147.85] | K |
|
| Tfus | Outlier 147.85 | K | Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol |
| Tfus | 146.35 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 146.58 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 146.50 | K | KDB |
| Tfus | 146.50 | K | Aq. Solubility Prediction |
| Tfus | 146.55 | K | NIST |
| Tfus | 146.65 | K | NIST |
| Tfus | 146.55 ± 0.05 | K | NIST |
| Tfus | 146.81 ± 0.15 | K | NIST |
| Tfus | 146.55 ± 0.01 | K | NIST |
| Tfus | 146.67 ± 0.10 | K | NIST |
| Tfus | Outlier 144.00 ± 4.00 | K | NIST |
| Tfus | 146.75 ± 0.30 | K | NIST |
| Tfus | 146.75 ± 1.50 | K | NIST |
| Tfus | 147.00 ± 2.00 | K | NIST |
| Tfus | 146.85 ± 0.40 | K | NIST |
| Tfus | 146.30 ± 1.00 | K | NIST |
| Tfus | 146.20 ± 2.00 | K | NIST |
| Tfus | 146.30 ± 0.10 | K | NIST |
| Tfus | 146.80 ± 0.50 | K | NIST |
| Tfus | 146.75 ± 0.30 | K | NIST |
| Ttriple | [146.57; 146.59] | K |
|
| Ttriple | 146.59 | K | Staveley, Lobo and Calado (1981), triple points Compiled value |
| Ttriple | 146.58 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 146.58 ± 0.05 | K | NIST |
| Ttriple | 146.57 ± 0.08 | K | NIST |
| Ttriple | 146.58 ± 0.05 | K | NIST |
| Ttriple | 146.57 ± 0.08 | K | NIST |
| UQi | 3.78 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.72 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.368; 0.369] | m3/kmol |
|
| Vc | 0.369 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Vc | 0.369 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.368 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.369 | m3/kmol | KDB |
| Vc | 0.369 | m3/kmol | NIST |
| VCOSTALD | 0.37 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.24 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | [0.2680000; 0.2700000] |
|
|
| Zc | 0.2700000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value | |
| Zc | 0.2680000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2699580 | KDB | |
| Zra | [0.27; 0.27] |
|
|
| Zra | 0.27 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 410.00 | 200000.00 | 812.647 |
| 410.00 | 180000.00 | 804.482 |
| 410.00 | 160000.00 | 795.899 |
| 410.00 | 140000.00 | 786.383 |
| 410.00 | 120000.00 | 776.018 |
| 410.00 | 100000.00 | 764.111 |
| 410.00 | 90000.00 | 757.777 |
| 410.00 | 80000.00 | 750.846 |
| 410.00 | 70000.00 | 743.853 |
| 410.00 | 60000.00 | 736.124 |
| 410.00 | 50000.00 | 727.698 |
| 410.00 | 40000.00 | 717.821 |
| 410.00 | 30000.00 | 707.272 |
| 410.00 | 20000.00 | 695.044 |
| 450.00 | 200000.00 | 798.897 |
| 450.00 | 180000.00 | 790.183 |
| 450.00 | 160000.00 | 780.708 |
| 450.00 | 140000.00 | 770.433 |
| 450.00 | 120000.00 | 759.037 |
| 450.00 | 100000.00 | 746.296 |
| 450.00 | 90000.00 | 739.304 |
| 450.00 | 80000.00 | 731.598 |
| 450.00 | 70000.00 | 723.281 |
| 450.00 | 60000.00 | 714.464 |
| 450.00 | 50000.00 | 704.34 |
| 450.00 | 40000.00 | 693.215 |
| 450.00 | 30000.00 | 680.595 |
| 450.00 | 20000.00 | 664.914 |
| 500.00 | 200000.00 | 779.786 |
| 500.00 | 180000.00 | 770.353 |
| 500.00 | 160000.00 | 759.878 |
| 500.00 | 140000.00 | 748.645 |
| 500.00 | 120000.00 | 735.845 |
| 500.00 | 100000.00 | 721.454 |
| 500.00 | 90000.00 | 713.602 |
| 500.00 | 80000.00 | 704.872 |
| 500.00 | 70000.00 | 695.54 |
| 500.00 | 60000.00 | 684.828 |
| 500.00 | 50000.00 | 672.946 |
| 500.00 | 40000.00 | 659.481 |
| 500.00 | 30000.00 | 643.213 |
| 500.00 | 20000.00 | 623.145 |
| 550.00 | 200000.00 | 760.464 |
| 550.00 | 180000.00 | 750.159 |
| 550.00 | 160000.00 | 739.33 |
| 550.00 | 140000.00 | 726.911 |
| 550.00 | 120000.00 | 713.086 |
| 550.00 | 100000.00 | 697.29 |
| 550.00 | 90000.00 | 688.637 |
| 550.00 | 80000.00 | 678.738 |
| 550.00 | 70000.00 | 668.08 |
| 550.00 | 60000.00 | 656.179 |
| 550.00 | 50000.00 | 642.447 |
| 550.00 | 40000.00 | 626.206 |
| 550.00 | 30000.00 | 605.816 |
| 550.00 | 20000.00 | 579.029 |
| 600.00 | 200000.00 | 741.384 |
| 600.00 | 180000.00 | 730.911 |
| 600.00 | 160000.00 | 718.93 |
| 600.00 | 140000.00 | 705.698 |
| 600.00 | 120000.00 | 690.895 |
| 600.00 | 100000.00 | 673.632 |
| 600.00 | 90000.00 | 664.012 |
| 600.00 | 80000.00 | 653.239 |
| 600.00 | 70000.00 | 641.114 |
| 600.00 | 60000.00 | 627.511 |
| 600.00 | 50000.00 | 611.576 |
| 600.00 | 40000.00 | 592.364 |
| 600.00 | 30000.00 | 567.711 |
| 600.00 | 20000.00 | 532.582 |
| 600.00 | 12000.00 | 485.331 |
| 410.00 | 10000.00 | 680.503 |
| 450.00 | 10000.00 | 645.737 |
| 500.00 | 10000.00 | 595.224 |
| 550.00 | 10000.00 | 537.032 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 777.6 |
| 283.15 | 5000.00 | 781.4 |
| 283.15 | 10000.00 | 785.2 |
| 283.15 | 15000.00 | 788.7 |
| 283.15 | 20000.00 | 792.1 |
| 283.15 | 25000.00 | 795.3 |
| 283.15 | 30000.00 | 798.5 |
| 283.15 | 35000.00 | 801.5 |
| 283.15 | 40000.00 | 804.4 |
| 283.15 | 45000.00 | 807.3 |
| 293.15 | 100.00 | 769.0 |
| 293.15 | 5000.00 | 773.0 |
| 293.15 | 10000.00 | 777.0 |
| 293.15 | 15000.00 | 780.7 |
| 293.15 | 20000.00 | 784.3 |
| 293.15 | 25000.00 | 787.8 |
| 293.15 | 30000.00 | 791.1 |
| 293.15 | 35000.00 | 794.2 |
| 293.15 | 40000.00 | 797.3 |
| 293.15 | 45000.00 | 800.2 |
| 303.15 | 100.00 | 760.4 |
| 303.15 | 5000.00 | 764.7 |
| 303.15 | 10000.00 | 768.9 |
| 303.15 | 15000.00 | 772.8 |
| 303.15 | 20000.00 | 776.6 |
| 303.15 | 25000.00 | 780.2 |
| 303.15 | 30000.00 | 783.7 |
| 303.15 | 35000.00 | 787.0 |
| 303.15 | 40000.00 | 790.2 |
| 303.15 | 45000.00 | 793.3 |
| 313.15 | 100.00 | 751.7 |
| 313.15 | 5000.00 | 756.2 |
| 313.15 | 10000.00 | 760.7 |
| 313.15 | 15000.00 | 764.8 |
| 313.15 | 20000.00 | 768.8 |
| 313.15 | 25000.00 | 772.7 |
| 313.15 | 30000.00 | 776.3 |
| 313.15 | 35000.00 | 779.8 |
| 313.15 | 40000.00 | 783.1 |
| 313.15 | 45000.00 | 786.4 |
| 323.15 | 100.00 | 742.9 |
| 323.15 | 5000.00 | 747.7 |
| 323.15 | 10000.00 | 752.5 |
| 323.15 | 15000.00 | 756.9 |
| 323.15 | 20000.00 | 761.1 |
| 323.15 | 25000.00 | 765.1 |
| 323.15 | 30000.00 | 769.0 |
| 323.15 | 35000.00 | 772.6 |
| 323.15 | 40000.00 | 776.1 |
| 323.15 | 45000.00 | 779.5 |
| 333.15 | 100.00 | 733.9 |
| 333.15 | 5000.00 | 739.0 |
| 333.15 | 10000.00 | 744.1 |
| 333.15 | 15000.00 | 748.8 |
| 333.15 | 20000.00 | 753.3 |
| 333.15 | 25000.00 | 757.5 |
| 333.15 | 30000.00 | 761.5 |
| 333.15 | 35000.00 | 765.4 |
| 333.15 | 40000.00 | 769.0 |
| 333.15 | 45000.00 | 772.5 |
| 343.15 | 100.00 | 724.8 |
| 343.15 | 5000.00 | 730.4 |
| 343.15 | 10000.00 | 735.8 |
| 343.15 | 15000.00 | 740.8 |
| 343.15 | 20000.00 | 745.6 |
| 343.15 | 25000.00 | 750.0 |
| 343.15 | 30000.00 | 754.2 |
| 343.15 | 35000.00 | 758.2 |
| 343.15 | 40000.00 | 762.1 |
| 343.15 | 45000.00 | 765.7 |
| 353.15 | 100.00 | 715.7 |
| 353.15 | 5000.00 | 721.7 |
| 353.15 | 10000.00 | 727.4 |
| 353.15 | 15000.00 | 732.8 |
| 353.15 | 20000.00 | 737.8 |
| 353.15 | 25000.00 | 742.5 |
| 353.15 | 30000.00 | 747.0 |
| 353.15 | 35000.00 | 751.2 |
| 353.15 | 40000.00 | 755.2 |
| 353.15 | 45000.00 | 759.0 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Thermal conductivity, W/m/K - Liquid |
| 96.00 | 302.00 | 0.1056 |
| 96.00 | 302.48 | 0.1054 |
| 96.00 | 303.02 | 0.1052 |
| 97.00 | 301.17 | 0.1058 |
| 97.00 | 301.56 | 0.1057 |
| 125.00 | 321.59 | 0.1008 |
| 128.00 | 321.98 | 0.1007 |
| 129.00 | 322.42 | 0.1005 |
| 132.00 | 322.90 | 0.1004 |
| 134.00 | 323.43 | 0.1003 |
| 140.00 | 381.25 | 0.0877 |
| 144.00 | 381.66 | 0.0876 |
| 148.00 | 382.09 | 0.0875 |
| 151.00 | 382.58 | 0.0874 |
| 157.00 | 383.11 | 0.0873 |
| 159.00 | 340.09 | 0.0964 |
| 179.00 | 340.50 | 0.0964 |
| 199.00 | 340.97 | 0.0963 |
| 213.00 | 360.16 | 0.0921 |
| 216.00 | 341.47 | 0.0961 |
| 229.00 | 342.02 | 0.0960 |
| 229.00 | 360.59 | 0.0920 |
| 246.00 | 361.06 | 0.0918 |
| 262.00 | 361.56 | 0.0917 |
| 319.00 | 360.24 | 0.0921 |
| 338.00 | 360.65 | 0.0920 |
| 354.00 | 361.12 | 0.0919 |
| 371.00 | 361.62 | 0.0918 |
| 389.00 | 362.14 | 0.0917 |
| 4974.00 | 301.55 | 0.1075 |
| 4975.00 | 301.16 | 0.1076 |
| 4981.00 | 301.98 | 0.1074 |
| 4988.00 | 302.46 | 0.1071 |
| 4995.00 | 302.99 | 0.1071 |
| 5052.00 | 323.39 | 0.1023 |
| 5053.00 | 322.87 | 0.1024 |
| 5058.00 | 322.40 | 0.1026 |
| 5065.00 | 321.59 | 0.1028 |
| 5066.00 | 321.97 | 0.1027 |
| 5170.00 | 340.29 | 0.0986 |
| 5183.00 | 340.70 | 0.0985 |
| 5196.00 | 341.15 | 0.0985 |
| 5209.00 | 341.64 | 0.0983 |
| 5221.00 | 342.17 | 0.0981 |
| 5232.00 | 381.28 | 0.0903 |
| 5239.00 | 381.67 | 0.0902 |
| 5242.00 | 382.15 | 0.0901 |
| 5246.00 | 382.61 | 0.0900 |
| 5250.00 | 383.12 | 0.0899 |
| 5318.00 | 360.52 | 0.0944 |
| 5334.00 | 360.93 | 0.0944 |
| 5344.00 | 361.38 | 0.0942 |
| 5355.00 | 361.86 | 0.0941 |
| 5370.00 | 362.40 | 0.0939 |
| 10060.00 | 323.35 | 0.1043 |
| 10073.00 | 322.84 | 0.1044 |
| 10074.00 | 321.58 | 0.1048 |
| 10075.00 | 321.96 | 0.1047 |
| 10077.00 | 322.37 | 0.1046 |
| 10174.00 | 381.41 | 0.0926 |
| 10175.00 | 360.80 | 0.0966 |
| 10177.00 | 381.79 | 0.0925 |
| 10181.00 | 382.20 | 0.0925 |
| 10185.00 | 382.65 | 0.0924 |
| 10187.00 | 361.19 | 0.0965 |
| 10191.00 | 383.16 | 0.0922 |
| 10202.00 | 361.63 | 0.0963 |
| 10214.00 | 362.05 | 0.0962 |
| 10220.00 | 362.58 | 0.0961 |
| 10264.00 | 301.15 | 0.1095 |
| 10268.00 | 301.53 | 0.1094 |
| 10276.00 | 301.96 | 0.1093 |
| 10282.00 | 302.42 | 0.1091 |
| 10285.00 | 302.94 | 0.1091 |
| 10297.00 | 340.62 | 0.1007 |
| 10311.00 | 341.02 | 0.1006 |
| 10324.00 | 341.36 | 0.1005 |
| 10336.00 | 341.88 | 0.1004 |
| 10348.00 | 342.41 | 0.1002 |
| 15046.00 | 322.36 | 0.1064 |
| 15047.00 | 322.81 | 0.1063 |
| 15051.00 | 321.94 | 0.1065 |
| 15052.00 | 323.31 | 0.1062 |
| 15067.00 | 321.56 | 0.1066 |
| 15359.00 | 301.13 | 0.1112 |
| 15364.00 | 301.51 | 0.1112 |
| 15367.00 | 301.93 | 0.1111 |
| 15369.00 | 302.39 | 0.1109 |
| 15369.00 | 302.91 | 0.1108 |
| 20077.00 | 381.47 | 0.0970 |
| 20079.00 | 381.83 | 0.0969 |
| 20080.00 | 382.23 | 0.0969 |
| 20083.00 | 382.66 | 0.0967 |
| 20089.00 | 383.14 | 0.0966 |
| 20101.00 | 301.49 | 0.1128 |
| 20103.00 | 301.91 | 0.1127 |
| 20105.00 | 302.37 | 0.1126 |
| 20106.00 | 301.12 | 0.1129 |
| 20111.00 | 302.87 | 0.1124 |
| 20118.00 | 323.27 | 0.1080 |
| 20122.00 | 322.77 | 0.1081 |
| 20134.00 | 322.33 | 0.1083 |
| 20137.00 | 321.55 | 0.1084 |
| 20140.00 | 321.92 | 0.1084 |
| 20146.00 | 360.98 | 0.1007 |
| 20163.00 | 361.36 | 0.1005 |
| 20175.00 | 361.78 | 0.1004 |
| 20185.00 | 362.23 | 0.1003 |
| 20191.00 | 362.73 | 0.1002 |
| 20284.00 | 340.69 | 0.1046 |
| 20295.00 | 341.08 | 0.1045 |
| 20305.00 | 341.50 | 0.1044 |
| 20315.00 | 341.96 | 0.1043 |
| 20326.00 | 342.45 | 0.1041 |
| 20779.00 | 401.40 | 0.0939 |
| 20781.00 | 402.98 | 0.0937 |
| 20783.00 | 401.69 | 0.0940 |
| 20786.00 | 402.08 | 0.0940 |
| 20788.00 | 402.50 | 0.0939 |
| 25201.00 | 321.53 | 0.1102 |
| 25206.00 | 321.90 | 0.1101 |
| 25213.00 | 322.30 | 0.1100 |
| 25216.00 | 322.74 | 0.1099 |
| 25218.00 | 323.23 | 0.1098 |
| 25356.00 | 301.48 | 0.1146 |
| 25356.00 | 301.89 | 0.1144 |
| 25357.00 | 301.11 | 0.1146 |
| 25365.00 | 302.34 | 0.1143 |
| 25376.00 | 302.83 | 0.1141 |
| 30060.00 | 401.62 | 0.0977 |
| 30061.00 | 401.28 | 0.0978 |
| 30061.00 | 402.00 | 0.0978 |
| 30062.00 | 402.40 | 0.0976 |
| 30065.00 | 402.86 | 0.0976 |
| 30157.00 | 301.10 | 0.1161 |
| 30163.00 | 301.45 | 0.1161 |
| 30166.00 | 381.53 | 0.1009 |
| 30168.00 | 381.88 | 0.1009 |
| 30170.00 | 382.26 | 0.1008 |
| 30172.00 | 382.68 | 0.1008 |
| 30173.00 | 301.86 | 0.1160 |
| 30175.00 | 383.14 | 0.1006 |
| 30178.00 | 302.31 | 0.1158 |
| 30182.00 | 302.80 | 0.1157 |
| 30197.00 | 361.13 | 0.1044 |
| 30204.00 | 361.49 | 0.1046 |
| 30214.00 | 361.94 | 0.1042 |
| 30229.00 | 362.37 | 0.1041 |
| 30238.00 | 321.51 | 0.1120 |
| 30240.00 | 362.86 | 0.1040 |
| 30245.00 | 321.87 | 0.1119 |
| 30247.00 | 322.27 | 0.1118 |
| 30248.00 | 322.70 | 0.1117 |
| 30250.00 | 323.18 | 0.1115 |
| 30916.00 | 340.82 | 0.1084 |
| 30924.00 | 341.19 | 0.1083 |
| 30924.00 | 342.03 | 0.1080 |
| 30929.00 | 341.58 | 0.1082 |
| 30930.00 | 342.52 | 0.1080 |
| 35184.00 | 321.89 | 0.1136 |
| 35184.00 | 322.28 | 0.1134 |
| 35187.00 | 322.71 | 0.1132 |
| 35189.00 | 321.54 | 0.1135 |
| 35194.00 | 323.19 | 0.1131 |
| 35410.00 | 302.81 | 0.1173 |
| 35412.00 | 301.12 | 0.1177 |
| 35412.00 | 302.32 | 0.1173 |
| 35414.00 | 301.88 | 0.1176 |
| 35415.00 | 301.48 | 0.1177 |
| 39278.00 | 302.78 | 0.1184 |
| 39375.00 | 302.30 | 0.1186 |
| 39484.00 | 301.86 | 0.1188 |
| 39611.00 | 301.45 | 0.1189 |
| 39719.00 | 301.10 | 0.1190 |
| 40156.00 | 361.31 | 0.1079 |
| 40156.00 | 361.66 | 0.1078 |
| 40164.00 | 362.05 | 0.1078 |
| 40170.00 | 362.47 | 0.1076 |
| 40176.00 | 362.93 | 0.1076 |
| 40251.00 | 340.96 | 0.1114 |
| 40255.00 | 382.26 | 0.1045 |
| 40256.00 | 381.56 | 0.1047 |
| 40257.00 | 382.67 | 0.1044 |
| 40259.00 | 381.89 | 0.1046 |
| 40259.00 | 383.12 | 0.1044 |
| 40260.00 | 341.32 | 0.1114 |
| 40269.00 | 341.72 | 0.1114 |
| 40272.00 | 342.62 | 0.1111 |
| 40276.00 | 342.14 | 0.1113 |
| 40385.00 | 323.14 | 0.1148 |
| 40395.00 | 321.51 | 0.1153 |
| 40397.00 | 322.25 | 0.1150 |
| 40398.00 | 321.86 | 0.1151 |
| 40399.00 | 322.67 | 0.1149 |
| 40492.00 | 401.21 | 0.1018 |
| 40492.00 | 401.53 | 0.1017 |
| 40496.00 | 401.89 | 0.1017 |
| 40498.00 | 402.28 | 0.1017 |
| 40498.00 | 402.71 | 0.1015 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [97.56; 432.52] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 8.29020e+01 | |||
| Coefficient B | -8.04580e+02 | |||
| Coefficient C | 6.78924e+00 | |||
| Coefficient D | -4.29770e-04 | |||
| Coefficient E | 1.10510e-07 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 97.56 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 157.97 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 225.47 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 281.44 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 324.52 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 357.27 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 382.45 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 402.32 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 418.59 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 432.52 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [139.51; 194.29] | J/mol×K | [146.58; 320.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.21540e+02 | |||
| Coefficient B | -7.03020e+00 | |||
| Coefficient C | 1.28924e+00 | |||
| Coefficient D | 1.27610e-02 | |||
| Coefficient E | -1.03880e-05 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 320.00 | |||
| Cp,liquid | 139.51 | J/mol×K | 146.58 | Calculated Property |
| Cp,liquid | 143.24 | J/mol×K | 165.85 | Calculated Property |
| Cp,liquid | 147.53 | J/mol×K | 185.12 | Calculated Property |
| Cp,liquid | 152.39 | J/mol×K | 204.39 | Calculated Property |
| Cp,liquid | 157.86 | J/mol×K | 223.66 | Calculated Property |
| Cp,liquid | 163.94 | J/mol×K | 242.92 | Calculated Property |
| Cp,liquid | 170.65 | J/mol×K | 262.19 | Calculated Property |
| Cp,liquid | 177.97 | J/mol×K | 281.46 | Calculated Property |
| Cp,liquid | 185.87 | J/mol×K | 300.73 | Calculated Property |
| Cp,liquid | 194.29 | J/mol×K | 320.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0458503; 0.0001650] | Pa×s | [146.58; 457.68] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.14110e+01 | |||
| Coefficient B | 1.21430e+03 | |||
| Coefficient C | 9.04570e-03 | |||
| Coefficient D | -3.27000e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 457.68 | |||
| η | 0.0458503 | Pa×s | 146.58 | Calculated Property |
| η | 0.0094510 | Pa×s | 181.15 | Calculated Property |
| η | 0.0032319 | Pa×s | 215.71 | Calculated Property |
| η | 0.0014865 | Pa×s | 250.28 | Calculated Property |
| η | 0.0008255 | Pa×s | 284.85 | Calculated Property |
| η | 0.0005206 | Pa×s | 319.41 | Calculated Property |
| η | 0.0003592 | Pa×s | 353.98 | Calculated Property |
| η | 0.0002647 | Pa×s | 388.55 | Calculated Property |
| η | 0.0002051 | Pa×s | 423.11 | Calculated Property |
| η | 0.0001650 | Pa×s | 457.68 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [44.62; 1.33] | kJ/mol | [146.58; 572.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.37410e+01 | |||
| Coefficient B | 6.56980e-01 | |||
| Coefficient C | 5.08750e-03 | |||
| Coefficient D | -5.30820e-01 | |||
| Coefficient E | 2.91490e-01 | |||
| Critical temperature, Tc (K) | 5.72190e+02 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 572.10 | |||
| ΔvapH | 44.62 | kJ/mol | 146.58 | Calculated Property |
| ΔvapH | 41.77 | kJ/mol | 193.86 | Calculated Property |
| ΔvapH | 38.98 | kJ/mol | 241.14 | Calculated Property |
| ΔvapH | 36.24 | kJ/mol | 288.42 | Calculated Property |
| ΔvapH | 33.46 | kJ/mol | 335.70 | Calculated Property |
| ΔvapH | 30.56 | kJ/mol | 382.98 | Calculated Property |
| ΔvapH | 27.35 | kJ/mol | 430.26 | Calculated Property |
| ΔvapH | 23.45 | kJ/mol | 477.54 | Calculated Property |
| ΔvapH | 17.96 | kJ/mol | 524.82 | Calculated Property |
| ΔvapH | 1.33 | kJ/mol | 572.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [269.44; 400.29] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41079e+01 | |||
| Coefficient B | -3.16636e+03 | |||
| Coefficient C | -4.03310e+01 | |||
| Temperature range, min. | 269.44 | |||
| Temperature range, max. | 400.29 | |||
| Pvap | 1.33 | kPa | 269.44 | Calculated Property |
| Pvap | 3.04 | kPa | 283.98 | Calculated Property |
| Pvap | 6.32 | kPa | 298.52 | Calculated Property |
| Pvap | 12.16 | kPa | 313.06 | Calculated Property |
| Pvap | 21.88 | kPa | 327.60 | Calculated Property |
| Pvap | 37.20 | kPa | 342.13 | Calculated Property |
| Pvap | 60.25 | kPa | 356.67 | Calculated Property |
| Pvap | 93.54 | kPa | 371.21 | Calculated Property |
| Pvap | 139.93 | kPa | 385.75 | Calculated Property |
| Pvap | 202.63 | kPa | 400.29 | Calculated Property |
| Pvap | [2.26e-07; 3464.07] | kPa | [146.58; 572.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.71175e+01 | |||
| Coefficient B | -6.72008e+03 | |||
| Coefficient C | -9.36745e+00 | |||
| Coefficient D | 6.89253e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 572.10 | |||
| Pvap | 2.26e-07 | kPa | 146.58 | Calculated Property |
| Pvap | 1.32e-03 | kPa | 193.86 | Calculated Property |
| Pvap | 0.18 | kPa | 241.14 | Calculated Property |
| Pvap | 3.78 | kPa | 288.42 | Calculated Property |
| Pvap | 29.76 | kPa | 335.70 | Calculated Property |
| Pvap | 129.57 | kPa | 382.98 | Calculated Property |
| Pvap | 390.31 | kPa | 430.26 | Calculated Property |
| Pvap | 927.52 | kPa | 477.54 | Calculated Property |
| Pvap | 1886.64 | kPa | 524.82 | Calculated Property |
| Pvap | 3464.07 | kPa | 572.10 | Calculated Property |
| Pvap | [1.52e-07; 3503.44] | kPa | [146.58; 572.19] |
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 | 8.72968e+01 | |||
| Coefficient B | -7.12610e+03 | |||
| Coefficient C | -1.09404e+01 | |||
| Coefficient D | 8.50410e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 572.19 | |||
| Pvap | 1.52e-07 | kPa | 146.58 | Calculated Property |
| Pvap | 1.15e-03 | kPa | 193.87 | Calculated Property |
| Pvap | 0.17 | kPa | 241.16 | Calculated Property |
| Pvap | 3.77 | kPa | 288.45 | Calculated Property |
| Pvap | 29.89 | kPa | 335.74 | Calculated Property |
| Pvap | 129.73 | kPa | 383.03 | Calculated Property |
| Pvap | 388.94 | kPa | 430.32 | Calculated Property |
| Pvap | 922.92 | kPa | 477.61 | Calculated Property |
| Pvap | 1885.63 | kPa | 524.90 | Calculated Property |
| Pvap | 3503.44 | kPa | 572.19 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [882.72; 269.64] | kg/m3 | [146.58; 572.10] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 5.39964e+01 | |||
| Coefficient B | 2.34760e-01 | |||
| Coefficient C | 5.72190e+02 | |||
| Coefficient D | 2.52370e-01 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 572.10 | |||
| ρl | 882.72 | kg/m3 | 146.58 | Calculated Property |
| ρl | 848.63 | kg/m3 | 193.86 | Calculated Property |
| ρl | 812.71 | kg/m3 | 241.14 | Calculated Property |
| ρl | 774.51 | kg/m3 | 288.42 | Calculated Property |
| ρl | 733.37 | kg/m3 | 335.70 | Calculated Property |
| ρl | 688.27 | kg/m3 | 382.98 | Calculated Property |
| ρl | 637.44 | kg/m3 | 430.26 | Calculated Property |
| ρl | 577.31 | kg/m3 | 477.54 | Calculated Property |
| ρl | 498.14 | kg/m3 | 524.82 | Calculated Property |
| ρl | 269.64 | kg/m3 | 572.10 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.01] | N/m | [146.55; 374.05] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.69759e-02 | |||
| Coefficient B | -1.13000e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 146.55 | |||
| Temperature range, max. | 374.05 | |||
| γ | 0.04 | N/m | 146.55 | Calculated Property |
| γ | 0.04 | N/m | 171.83 | Calculated Property |
| γ | 0.03 | N/m | 197.11 | Calculated Property |
| γ | 0.03 | N/m | 222.38 | Calculated Property |
| γ | 0.03 | N/m | 247.66 | Calculated Property |
| γ | 0.03 | N/m | 272.94 | Calculated Property |
| γ | 0.02 | N/m | 298.22 | Calculated Property |
| γ | 0.02 | N/m | 323.49 | Calculated Property |
| γ | 0.02 | N/m | 348.77 | Calculated Property |
| γ | 0.01 | N/m | 374.05 | Calculated Property |
| γ | [0.04; 4.65e-06] | N/m | [146.58; 566.99] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -7.10520e-03 | |||
| Coefficient B | 3.71920e+01 | |||
| Coefficient C | -3.22680e+00 | |||
| Coefficient D | 7.37700e-04 | |||
| Coefficient E | -6.85370e-06 | |||
| Comment | Range stopped where the equation turns negative; ChemSep gives it to 572.1 K. | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 566.99 | |||
| γ | 0.04 | N/m | 146.58 | Calculated Property |
| γ | 0.04 | N/m | 193.29 | Calculated Property |
| γ | 0.03 | N/m | 240.01 | Calculated Property |
| γ | 0.02 | N/m | 286.72 | Calculated Property |
| γ | 0.02 | N/m | 333.43 | Calculated Property |
| γ | 0.01 | N/m | 380.14 | Calculated Property |
| γ | 0.01 | N/m | 426.86 | Calculated Property |
| γ | 0.01 | N/m | 473.57 | Calculated Property |
| γ | 0.00 | N/m | 520.28 | Calculated Property |
| γ | 4.65e-06 | N/m | 566.99 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.10] | W/m×K | [146.58; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 7.47540e-05 | |||
| Coefficient B | 1.11900e+00 | |||
| Coefficient C | 6.13150e+02 | |||
| Coefficient D | 2.28820e+04 | |||
| Temperature range, min. | 146.58 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 146.58 | Calculated Property |
| λgas | 0.01 | W/m×K | 241.40 | Calculated Property |
| λgas | 0.02 | W/m×K | 336.23 | Calculated Property |
| λgas | 0.03 | W/m×K | 431.05 | Calculated Property |
| λgas | 0.04 | W/m×K | 525.88 | Calculated Property |
| λgas | 0.05 | W/m×K | 620.70 | Calculated Property |
| λgas | 0.06 | W/m×K | 715.53 | Calculated Property |
| λgas | 0.08 | W/m×K | 810.35 | Calculated Property |
| λgas | 0.09 | W/m×K | 905.18 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.12; 0.09] | W/m×K | [273.15; 374.08] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 3.57710e-02 | |||
| Coefficient B | -2.49640e+02 | |||
| Coefficient C | 1.09040e-01 | |||
| Coefficient D | -6.65670e-03 | |||
| Coefficient E | 1.39370e-06 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 374.08 | |||
| λliquid | 0.12 | W/m×K | 273.15 | Calculated Property |
| λliquid | 0.11 | W/m×K | 284.36 | Calculated Property |
| λliquid | 0.11 | W/m×K | 295.58 | Calculated Property |
| λliquid | 0.11 | W/m×K | 306.79 | Calculated Property |
| λliquid | 0.11 | W/m×K | 318.01 | Calculated Property |
| λliquid | 0.10 | W/m×K | 329.22 | Calculated Property |
| λliquid | 0.10 | W/m×K | 340.44 | Calculated Property |
| λliquid | 0.10 | W/m×K | 351.65 | Calculated Property |
| λliquid | 0.10 | W/m×K | 362.87 | Calculated Property |
| λliquid | 0.09 | W/m×K | 374.08 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexane, methyl-.
Mixtures
- Aniline + Cyclohexane, methyl- + Water
- Cyclohexylamine + Cyclohexane, methyl- + Water
- Aniline + Cyclohexylamine + Cyclohexane, methyl-
- Formamide, N,N-dimethyl- + Cyclohexane, methyl-
- Thiophene, 3-methyl- + Cyclohexane, methyl-
- Ethanol + Cyclohexane, methyl- + Pentane, 3-methyl-
- 2-Propanol, 2-methyl- + Ethanol + Cyclohexane, methyl-
- Cyclohexane, methyl- + Propanoic acid + Water
- Ethanol, 2-methoxy- + Cyclohexane, methyl-
- Ethanol, 2-ethoxy- + Cyclohexane, methyl-
- Toluene + Cyclohexane, methyl-
- Cyclohexane, methyl- + Thiophene, tetrahydro-, 1,1-dioxide
- Ethanol + Cyclohexane, methyl-
- 2-Propanol + Cyclohexane, methyl-
- 2-Pentanol + Cyclohexane, methyl-
- 2-Hexanol + Cyclohexane, methyl-
- 2-Heptanol + Cyclohexane, methyl-
- Dimethyl Sulfoxide + Cyclohexane, methyl-
- Cyclohexane, methyl- + Water
- Methane + Cyclohexane, methyl- + Water
Find more mixtures with Cyclohexane, methyl-.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Hankinson and Thomson (1979), COSTALD parameters ChEDL chemicals 1.5.2, from Hankinson, R. W.; Thomson, G. H. A New Correlation for Saturated Densities of Liquids and Their Mixtures. AIChE J. 1979, 25, 653-663.
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 ChEDL chemicals 1.5.2, from Daubert, T. E. Vapor-Liquid Critical Properties of Elements and Compounds. 5. Branched Alkanes and Cycloalkanes. J. Chem. Eng. Data 1996, 41, 365-372.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Staveley, Lobo and Calado (1981), triple points ChEDL chemicals 1.5.2, from Staveley, L. A. K.; Lobo, L. Q.; Calado, J. C. G. Triple-Points of Low Melting Substances and Their Use in Cryogenic Work. Cryogenics 1981, 21, 131-144.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Density of Methylcyclohexane at Temperatures up to 600 K and Pressures up to 200 MPa
- Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
- Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
- Liquid-liquid equilibrium data of water with neohexane, methylcyclohexane, tert-butyl methyl ether, n-heptane and vapor -liquid-liquid equilibrium with methane
- Liquid liquid equilibrium in ternary systems N,N-dimethylformamide + 2-methylpentane + methanol and N,N-dimethylformamide + methylcyclohexane + methanol
- Liquid liquid equilibria for the binary systems of sulfolane with branched cycloalkanes
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
- Liquid liquid equilibria of methylcyclohexane benzene N-formylmorpholine at several temperatures
- Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
- Isobaric vapor liquid equilibrium for ternary mixtures of ethanol and methylcyclohexane with 3-methylpentane and tert-butyl alcohol at 101.3 kPa
- Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
- Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
- Solubility of pyrene in simple and mixed solvent systems
- Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Application of [EMim][ESO4] ionic liquid as solvent in the extraction of toluene from cycloalkanes: Study of liquid-liquid equilibria at T = 298.15 K
- Measurement on vapor pressure, density and viscosity for binary mixtures of JP-10 and methylcyclohexane
- Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
- Ether + alcohol + hydrocarbon mixtures in fuels and bio-fuels: Excess enthalpies of binary mixtures containing dibutyl ether (DBE) or 1-butanol and 1-hexene or methylcyclohexane or toluene or cyclohexane or 2,2,4-trimethylpentane at 298.15K and 313.15K
- 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
- Experimental determination and correlation of tie line data for the system (water + butyric acid + methylcyclohexane) at four temperatures
- Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
- Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
- Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
- VLE and LLE in ternary systems of two associating components (water, aniline, and cyclohexylamine) and a hydrocarbon (cyclohexane or methylcyclohexane)
- Miscibility behavior of trihexyl(tetradecyl)phosphonium tetrafluoroborate with cyclic hydrocarbons
- Isobaric vapor-liquid equilibrium data for methylcyclohexane + 2-methoxyethanol and methylcyclohexane + 2-ethoxyethanol at 50.00 and 101.33 kPa
- (Liquid + liquid) equilibria in the (water + tetrahydrofuran + methylcyclohexane) ternary system at temperatures between (278 and 343) K and atmospheric pressure: Experimental data and correlation
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- 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
- 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
- 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
- (Liquid + liquid) phase behavior for systems containing (aromatic + TBA + methylcyclohexane)
- VLE of the binary systems (dimethyl carbonate with 2-propanol or 2-butanol) and (diethyl carbonate with methylcyclohexane) at 101.3 kPa
- Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
- Density measurements under pressure for the binary system (ethanol + methylcyclohexane)
- Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
- Tailor-made ionic liquids
- Speeds of sound, isentropic compressibilities, viscosities and excess molar volumes of binary mixtures of methylcyclohexane + 2-alkanols or ethanol at T = 298.15 K
- Physico-chemical and excess properties of the binary mixtures of methylcyclohexane + ethanol, + propan-1-ol, + propan-2-ol, + butan-1-ol, + 2-methyl-1-propanol, or 3-methyl-1-butanol at T = (298.15, 303.15, and 308.15) K
- Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
- Excess molar volumes, viscosities, and speeds of sound of the ternary mixture {1-heptanol (1) + trichloroethylene (2) + methylcyclohexane (3)} at T = 298.15 K
- (Liquid + liquid) equilibria for ternary mixtures of (water + propionic acid + organic solvent) at T = 303.2 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- Relation between characteristic molecular volume and hydrophobicity of nonpolar molecules
- Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
- Separation of toluene from cyclic hydrocarbons using 1-butyl-3-methylimidazolium methylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
- (Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
- Activity coefficients at infinite dilution 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
- Binary and ternary (liquid + liquid) equilibrium for {methylcyclohexane (1) + toluene (2) + 1-hexyl-3-methylimidazolium tetracyanoborate (3)/1-butyl-3-methylimidazolium tetracyanoborate (3)}
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Interactions of volatile organic compounds with 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 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- 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
- (Liquid + liquid) equilibrium data of (water + phosphoric acid + solvents) systems at T = (308.2 and 318.2) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- 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
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- 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
- 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
- Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
- 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
- Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
- Excess enthalpies of ternary mixtures of (oxygenated additives + cycloalkane) in fuels and bio-fuels: (dibutyl ether + 1-propanol + cyclohexane), or methylcyclohexane, at T = (298.15 and 313.15) K
- Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
- 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
- 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
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Measurement and correlation of density and viscosity of binary mixtures of fatty acid (methyl esters + methylcyclohexane)
- THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
- Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
- Measurement of Hydrogen Solubility in Potential Liquid Organic Hydrogen Carriers
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
- Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
- Density, Viscosity, and Freezing Point for Four Binary Systems of n-Dodecane or Methylcyclohexane Mixed with 1-Heptanol or Cyclohexylmethanol
- Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of n-Heptane + sec-Butyl Acetate and Methylcyclohexane + sec-Butyl Acetate under Atmosphere
- Liquid-Liquid Extraction of Cyclopentanone from Aqueous Solution with Methylcyclohexane or Propyl Acetate at Different Temperatures
- Densities, Viscosities, Speeds of Sound, Bulk Moduli, Surface Tensions, and Flash Points of Binary Mixtures of Ethylcyclohexane or Methylcyclohexane with n-Dodecane or n-Hexadecane at 0.1 MPa
- 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
- Isothermal Vapor-Liquid Equilibrium Data for Binary Systems of CHF3 or C2F6 with Methylcyclohexane or Toluene
- Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
- Isobaric Vapor-Liquid Equilibrium for Two Binary Systems of 3,3-Dimethyloxetane + Methyl Cyclohexane and 3-Chloro-2,2-dimethyl-1-propanol + Methyl Cyclohexane at 101.3 kPa
- Densities and Viscosities for the Ternary System of Decalin + Methylcyclohexane + Cyclopentanol and Corresponding Binaries at T = 293.15 to 343.15 K
- Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
- Isothermal Vapor-Liquid Equilibrium Data for the Binary Systems Consisting of 1,1,2,3,3,3-Hexafluoro-1-propene and Either Methylcyclohexane, Cyclohexane, n-Hexane, 2-Methyltetrahydrofuran, or 2,2,3,3,4,4,4-Heptafluoro-1-butanol
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Liquid-Liquid Equilibrium and Excess Enthalpies in Binary Systems Methylcyclohexane + Methanol and Methylcyclohexane + N,N-Dimethylformamide
- Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Branched Cycloalkanes
- Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
- Measurement and Correlation of Mutual Solubilities for High Viscosity Binary Systems: Aniline + Methylcyclohexane, Phenol + Heptane, Phenol + Octane, and Glycerol + 1-Pentanol
- High-Pressure Viscosity and Density Measurements of the Ternary System Methylcyclohexane + cis-Decalin + 2,2,4,4,6,8,8-Heptamethylnonane
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures of Ethanol, Methylcyclohexane and p-Xylene
- Solubilities of Alkylcyclohexanes in Water from 30 C to 180 C
- Density, Viscosity, and Speed of Sound of Dialkyl Carbonates with Cyclopentane and Methyl Cyclohexane at Several Temperatures
- Vapor-Liquid Equilibria for the Ternary Systems of Methyl tert-Butyl Ether + Methanol + Methylcyclohexane and Methyl tert-Butyl Ether + Methanol + n-Heptane and Constituent Binary Systems at 313.15 K
- Densities and Viscosities for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and Methylcyclohexane
- Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
- Shear Viscosities of Methycyclohexane, Perfluoromethylcyclohexane, and Their Mixtures in the Vicinity of the Upper Critical Mixing Temperature. 1. Critical Isopleth and Coexistence Curve
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
- Liquid Extraction of Benzene from Its Mixtures Using 1-Ethyl-3-methylimidazolium Ethylsulfate as a Solvent
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- 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
- Extraction of Benzene from Aliphatic Compounds Using Commercial Ionic Liquids as Solvents: Study of the Liquid Liquid Equilibrium at T = 298.15 K
- Densities and Viscosities of Binary and Ternary Mixtures of (Nitrobenzene + 1-Bromobutane), (1-Bromobutane + Methylcyclohexane), (Nitrobenzene + Methylcyclohexane), and (Methylcyclohexane + Nitrobenzene + 1-Bromobutane) from (293.15 to 308.15) K
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- 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
- Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
- Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Density, Viscosity, Refractive Index, and Freezing Point for Binary Mixtures of 1,1'-Bicyclohexyl with Alkylcyclohexane
- Experimental Study of Solubility of Water in Liquid Organic Hydrogen Carriers
- 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 and Correlation of Liquid-Liquid Equilibria of Methylcyclohexane + Toluene + N-Formylmorpholine at (293, 303, 313, and 323) K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- Measurement and Correlation of Liquid-Liquid Equilibria of Two Imidazolium Ionic Liquids with Thiophene and Methylcyclohexane
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurement and correlation of the thermal conductivity of methylcyclohexane and propylcyclohexane from 300 K to 600 K at pressures to 60 MPa
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
- Volumetric and Viscous Properties at Several Temperatures for Binary Mixtures of N-Methylpiperazine with Methylcyclohexane or n-Heptane
- 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
- Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
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