- InChI
- InChI=1S/C6H12/c1-2-4-6-5-3-1/h1-6H2
- InChI Key
- XDTMQSROBMDMFD-UHFFFAOYSA-N
- Formula
- C6H12
- SMILES
- C1CCCCC1
- Molecular Weight1
- 84.16
- CAS
- 110-82-7
- Other Names
-
- Benzene, hexahydro-
- Cicloesano
- Cykloheksan
- Hexahydrobenzene
- Hexamethylene
- Hexanaphthene
- NSC 406835
- Rcra waste number U056
- UN 1145
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- AP : Aniline Point (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).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- 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).
- 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.
- D*i : Self diffusion coefficient (m2/s).
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil(P) : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Vm : Molar Volume (m3/mol).
- VCOSTALD : COSTALD Characteristic Volume (m3/kmol).
- ωSRK : SRK acentric factor.
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2110; 0.2144] |
|
|
| ω | 0.2130 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.2144 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.2110 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.2120 | KDB | |
| PAff | 686.90 | kJ/mol | NIST |
| Tig | 543.15 | K | KDB |
| AP | 304.150 | K | KDB |
| BasG | 666.90 | kJ/mol | NIST |
| ΔcH°liquid | [-3947.00; -3918.00] | kJ/mol |
|
| ΔcH°liquid | -3918.60 ± 0.70 | kJ/mol | NIST |
| ΔcH°liquid | -3918.40 ± 1.00 | kJ/mol | NIST |
| ΔcH°liquid | -3919.90 ± 0.71 | kJ/mol | NIST |
| ΔcH°liquid | -3919.60 ± 1.30 | kJ/mol | NIST |
| ΔcH°liquid | -3918.00 ± 0.75 | kJ/mol | NIST |
| ΔcH°liquid | -3935.30 | kJ/mol | NIST |
| ΔcH°liquid | Outlier -3947.00 | kJ/mol | NIST |
| μ | [0.00; 0.30] | debye |
|
| μ | 0.00 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 0.30 | debye | KDB |
| η | 0.0008920 | Pa×s | Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K |
| LFL | 1.33 | % in Air | KDB |
| UFL | 8.35 | % in Air | KDB |
| Tflash,oc | 253.15 | K | KDB |
| ΔfG° | [31.78; 31.91] | kJ/mol |
|
| ΔfG° | 31.91 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 31.78 | kJ/mol | KDB |
| Rg | 3.2610 | KDB | |
| Δc,grossH | 3919.82 | kJ/mol | KDB |
| Δc,netH | 3655.770 | kJ/mol | KDB |
| ΔfH°gas | [-124.60; -122.08] | kJ/mol |
|
| ΔfH°gas | -122.08 ± 0.68 | kJ/mol | Active Thermochemical Tables 1.112, gas-phase enthalpies of formation Compiled value |
| ΔfH°gas | -123.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -123.20 | kJ/mol | KDB |
| ΔfH°gas | -124.60 | kJ/mol | NIST |
| ΔfH°gas | -123.10 ± 0.79 | kJ/mol | NIST |
| ΔfH°gas | -123.30 | kJ/mol | NIST |
| ΔfH°liquid | [-157.70; -156.20] | kJ/mol |
|
| ΔfH°liquid | -157.70 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -156.20 ± 0.79 | kJ/mol | NIST |
| ΔfH°liquid | -156.40 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 2.06 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.10; 33.50] | kJ/mol |
|
| ΔvapH° | 33.12 | kJ/mol | NIST |
| ΔvapH° | 33.10 | kJ/mol | NIST |
| ΔvapH° | 33.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 32.79 ± 0.14 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 33.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 32.90 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 32.90 | kJ/mol | NIST |
| ΔvapH° | 33.00 ± 0.02 | kJ/mol | NIST |
| ΔvapH° | 33.00 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | Outlier 30.10 | kJ/mol | NIST |
| ΔvapH° | 33.04 | kJ/mol | NIST |
| ΔvapH° | 33.50 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 33.03 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 33.10 | kJ/mol | NIST |
| ΔvapH° | 33.30 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 33.50 | kJ/mol | NIST |
| ΔvapH° | Outlier 30.20 ± 0.30 | kJ/mol | NIST |
| IE | [9.79; 11.00] | eV |
|
| IE | 9.88 ± 0.03 | eV | NIST |
| IE | 9.80 ± 0.05 | eV | NIST |
| IE | 10.00 ± 0.03 | eV | NIST |
| IE | 9.82 | eV | NIST |
| IE | 9.88 ± 0.10 | eV | NIST |
| IE | 9.88 | eV | NIST |
| IE | 9.88 ± 0.02 | eV | NIST |
| IE | 9.88 | eV | NIST |
| IE | 9.89 ± 0.01 | eV | NIST |
| IE | 9.83 ± 0.05 | eV | NIST |
| IE | 9.84 | eV | NIST |
| IE | 9.88 ± 0.01 | eV | NIST |
| IE | 9.87 | eV | NIST |
| IE | 9.88 ± 0.01 | eV | NIST |
| IE | 9.89 | eV | NIST |
| IE | 9.81 | eV | NIST |
| IE | 9.79 | eV | NIST |
| IE | 9.88 ± 0.02 | eV | NIST |
| IE | Outlier 11.00 ± 0.20 | eV | NIST |
| IE | 10.32 | eV | NIST |
| IE | 10.30 ± 0.10 | eV | NIST |
| IE | 10.30 | eV | NIST |
| log10WS | [-3.10; -3.10] |
|
|
| log10WS | -3.10 | Aq. Solubility Prediction | |
| log10WS | -3.10 | Estimated Solubility | |
| logPoct/wat | 2.341 | Crippen Calculated Property | |
| McVol | 84.540 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [4033.30; 4200.00] | kPa |
|
| Pc | 4060.00 | kPa | Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method |
| Pc | Outlier 4200.00 | kPa | Critical Properties of the Reacting Mixture in the Selective Oxidation of Cyclohexane by Oxygen in the Presence of Carbon Dioxide |
| Pc | 4080.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Pc | 4080.36 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4074.80 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 4073.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 4080.00 | kPa | KDB |
| Pc | 4080.00 ± 30.00 | kPa | NIST |
| Pc | 4071.00 ± 20.00 | kPa | NIST |
| Pc | 4075.00 ± 2.00 | kPa | NIST |
| Pc | 4097.00 ± 10.34 | kPa | NIST |
| Pc | 4036.00 ± 60.00 | kPa | NIST |
| Pc | 4110.76 ± 101.32 | kPa | NIST |
| Pc | 4036.70 ± 39.99 | kPa | NIST |
| Pc | 4033.30 ± 10.67 | kPa | NIST |
| Ptriple | [5.36; 5.40] | kPa |
|
| Ptriple | 5.36 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 5.40 | kPa | KDB |
| ρc | [271.84; 274.36] | kg/m3 |
|
| ρc | 272.68 ± 2.52 | kg/m3 | NIST |
| ρc | 274.36 ± 5.89 | kg/m3 | NIST |
| ρc | 271.84 ± 3.37 | kg/m3 | NIST |
| ρc | 273.52 ± 1.68 | kg/m3 | NIST |
| ρc | 273.27 ± 5.05 | kg/m3 | NIST |
| Inp | [619.00; 700.00] |
|
|
| Inp | 664.10 | NIST | |
| Inp | 660.10 | NIST | |
| Inp | 665.70 | NIST | |
| Inp | 662.30 | NIST | |
| Inp | 661.20 | NIST | |
| Inp | 661.90 | NIST | |
| Inp | 662.90 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 667.14 | NIST | |
| Inp | 667.02 | NIST | |
| Inp | 667.46 | NIST | |
| Inp | 656.80 | NIST | |
| Inp | 662.20 | NIST | |
| Inp | Outlier 693.60 | NIST | |
| Inp | 663.35 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | Outlier 688.30 | NIST | |
| Inp | Outlier 697.90 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 655.70 | NIST | |
| Inp | Outlier 692.80 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | Outlier 694.00 | NIST | |
| Inp | 660.60 | NIST | |
| Inp | 665.60 | NIST | |
| Inp | 660.60 | NIST | |
| Inp | 665.60 | NIST | |
| Inp | 662.70 | NIST | |
| Inp | 667.10 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 666.40 | NIST | |
| Inp | 671.10 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 658.70 | NIST | |
| Inp | 660.90 | NIST | |
| Inp | 663.20 | NIST | |
| Inp | 665.50 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 673.60 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 664.50 | NIST | |
| Inp | 666.80 | NIST | |
| Inp | 669.20 | NIST | |
| Inp | 671.70 | NIST | |
| Inp | 674.40 | NIST | |
| Inp | 677.30 | NIST | |
| Inp | 663.70 | NIST | |
| Inp | 664.20 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | Outlier 639.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 657.20 | NIST | |
| Inp | 659.60 | NIST | |
| Inp | 662.10 | NIST | |
| Inp | 664.70 | NIST | |
| Inp | 667.40 | NIST | |
| Inp | 670.30 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 659.10 | NIST | |
| Inp | 661.30 | NIST | |
| Inp | 663.60 | NIST | |
| Inp | 666.10 | NIST | |
| Inp | 668.80 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 669.20 | NIST | |
| Inp | 668.10 | NIST | |
| Inp | Outlier 690.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 662.70 | NIST | |
| Inp | 663.90 | NIST | |
| Inp | 662.78 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 668.80 | NIST | |
| Inp | 667.80 | NIST | |
| Inp | 675.60 | NIST | |
| Inp | 671.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | Outlier 689.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 675.70 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 663.80 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 674.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | Outlier 688.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 672.00 | NIST | |
| Inp | 656.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 667.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | Outlier 689.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | Outlier 688.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 678.00 | NIST | |
| Inp | 657.80 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 655.80 | NIST | |
| Inp | 647.56 | NIST | |
| Inp | 648.22 | NIST | |
| Inp | 656.20 | NIST | |
| Inp | 654.90 | NIST | |
| Inp | 655.40 | NIST | |
| Inp | 656.20 | NIST | |
| Inp | 657.60 | NIST | |
| Inp | 654.60 | NIST | |
| Inp | 655.40 | NIST | |
| Inp | 656.20 | NIST | |
| Inp | 657.60 | NIST | |
| Inp | 656.20 | NIST | |
| Inp | 654.90 | NIST | |
| Inp | 651.20 | NIST | |
| Inp | 651.24 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 651.09 | NIST | |
| Inp | 651.14 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 660.80 | NIST | |
| Inp | 657.30 | NIST | |
| Inp | 656.40 | NIST | |
| Inp | 647.36 | NIST | |
| Inp | 650.41 | NIST | |
| Inp | 652.19 | NIST | |
| Inp | 653.15 | NIST | |
| Inp | 656.24 | NIST | |
| Inp | 658.10 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | 648.90 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 673.00 | NIST | |
| Inp | 680.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 665.00 | NIST | |
| Inp | Outlier 619.00 | NIST | |
| Inp | Outlier 625.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | Outlier 688.00 | NIST | |
| Inp | 676.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 662.00 | NIST | |
| Inp | 654.90 | NIST | |
| Inp | 648.95 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 670.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 659.00 | NIST | |
| Inp | 660.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | Outlier 696.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 657.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 654.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 649.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 677.00 | NIST | |
| Inp | 666.00 | NIST | |
| Inp | 645.00 | NIST | |
| Inp | 661.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 664.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 675.00 | NIST | |
| Inp | 669.00 | NIST | |
| Inp | 663.00 | NIST | |
| Inp | 654.90 | NIST | |
| Inp | 655.40 | NIST | |
| Inp | 651.20 | NIST | |
| Inp | 651.00 | NIST | |
| Inp | 647.36 | NIST | |
| Inp | 658.10 | NIST | |
| Inp | 650.00 | NIST | |
| Inp | 658.00 | NIST | |
| Inp | 648.95 | NIST | |
| Inp | 668.00 | NIST | |
| Inp | 665.00 | NIST | |
| Ip | [712.00; 766.00] |
|
|
| Ip | 740.00 | NIST | |
| Ip | 766.00 | NIST | |
| Ip | 748.00 | NIST | |
| Ip | 752.00 | NIST | |
| Ip | 757.00 | NIST | |
| Ip | 740.00 | NIST | |
| Ip | 735.00 | NIST | |
| Ip | 742.00 | NIST | |
| Ip | 766.00 | NIST | |
| Ip | 726.00 | NIST | |
| Ip | 732.00 | NIST | |
| Ip | 738.00 | NIST | |
| Ip | 752.00 | NIST | |
| Ip | 722.00 | NIST | |
| Ip | 722.00 | NIST | |
| Ip | 722.00 | NIST | |
| Ip | 732.00 | NIST | |
| Ip | 734.00 | NIST | |
| Ip | 735.50 | NIST | |
| Ip | 737.00 | NIST | |
| Ip | 741.70 | NIST | |
| Ip | 723.00 | NIST | |
| Ip | 729.00 | NIST | |
| Ip | 729.00 | NIST | |
| Ip | 717.00 | NIST | |
| Ip | 712.00 | NIST | |
| Ip | 765.00 | NIST | |
| Ip | 742.00 | NIST | |
| Ip | 737.00 | NIST | |
| Ip | 765.00 | NIST | |
| Ip | 723.00 | NIST | |
| Ip | 756.00 | NIST | |
| Ip | 723.00 | NIST | |
| Ip | 726.00 | NIST | |
| Ip | 722.00 | NIST | |
| S°gas | 298.19 | J/mol×K | NIST |
| S°liquid | [203.89; 205.90] | J/mol×K |
|
| S°liquid | 203.89 | J/mol×K | NIST |
| S°liquid | 204.35 | J/mol×K | NIST |
| S°liquid | 205.90 | J/mol×K | NIST |
| Tboil | [342.10; 358.70] | K |
|
| Tboil | 353.73 | K | Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa |
| Tboil | 353.73 | K | Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa |
| Tboil | 353.70 | K | Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa |
| Tboil | 353.78 | K | A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures |
| Tboil | 355.00 | K | The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA |
| Tboil | 353.70 | K | Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K |
| Tboil | 353.94 | K | Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa |
| Tboil | 353.95 | K | Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K |
| Tboil | 353.82 | K | A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC) |
| Tboil | 353.85 | K | Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure |
| Tboil | 354.11 | K | Determination and Correlation of Vapor Liquid Equilibria for the Phosphoric Acid + Water + Cyclohexane + Ethanol System |
| Tboil | 353.82 | K | A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol |
| Tboil | 353.78 | K | Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa |
| Tboil | 353.73 | K | Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa |
| Tboil | 353.73 | K | Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa |
| Tboil | 353.90 | K | Isobaric Vapor-Liquid Equilibria for (Acetic Acid + Cyclohexane) and (Cyclohexane + Acetylacetone) at a Pressure of 101.3 kPa and for (Acetic Acid + Acetylacetone) at a Pressure of 60.0 kPa |
| Tboil | 353.93 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 353.88 | K | KDB |
| Tboil | 353.93 ± 0.10 | K | NIST |
| Tboil | 353.84 ± 0.10 | K | NIST |
| Tboil | 353.85 ± 0.20 | K | NIST |
| Tboil | 353.95 ± 0.10 | K | NIST |
| Tboil | 353.88 ± 0.20 | K | NIST |
| Tboil | 353.81 ± 0.15 | K | NIST |
| Tboil | 354.00 ± 1.00 | K | NIST |
| Tboil | 354.15 ± 0.30 | K | NIST |
| Tboil | 353.90 ± 0.08 | K | NIST |
| Tboil | 353.70 ± 0.30 | K | NIST |
| Tboil | 353.90 | K | NIST |
| Tboil | 353.25 ± 0.30 | K | NIST |
| Tboil | 353.25 ± 0.50 | K | NIST |
| Tboil | 353.25 ± 0.50 | K | NIST |
| Tboil | 353.88 ± 0.10 | K | NIST |
| Tboil | 353.90 | K | NIST |
| Tboil | 354.60 ± 0.30 | K | NIST |
| Tboil | 353.95 ± 0.20 | K | NIST |
| Tboil | 353.90 ± 0.40 | K | NIST |
| Tboil | 353.84 ± 0.20 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.25 ± 0.15 | K | NIST |
| Tboil | 354.00 ± 0.40 | K | NIST |
| Tboil | 353.90 ± 0.30 | K | NIST |
| Tboil | 353.25 ± 0.30 | K | NIST |
| Tboil | 354.00 ± 0.30 | K | NIST |
| Tboil | 353.95 ± 0.20 | K | NIST |
| Tboil | 353.91 ± 0.15 | K | NIST |
| Tboil | 353.85 ± 0.20 | K | NIST |
| Tboil | 353.95 ± 0.50 | K | NIST |
| Tboil | 353.40 ± 0.50 | K | NIST |
| Tboil | 353.90 ± 0.40 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.87 ± 0.01 | K | NIST |
| Tboil | 353.70 ± 0.10 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.87 ± 0.20 | K | NIST |
| Tboil | 353.89 ± 0.20 | K | NIST |
| Tboil | 354.00 ± 0.20 | K | NIST |
| Tboil | 353.70 ± 1.00 | K | NIST |
| Tboil | 353.88 ± 0.20 | K | NIST |
| Tboil | 353.89 ± 0.15 | K | NIST |
| Tboil | 353.85 ± 0.20 | K | NIST |
| Tboil | 354.15 ± 1.50 | K | NIST |
| Tboil | 353.85 ± 0.20 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.85 ± 0.30 | K | NIST |
| Tboil | 353.93 ± 0.30 | K | NIST |
| Tboil | 353.55 ± 0.30 | K | NIST |
| Tboil | 353.95 ± 0.50 | K | NIST |
| Tboil | 353.89 ± 0.40 | K | NIST |
| Tboil | 353.70 ± 2.00 | K | NIST |
| Tboil | 353.90 ± 0.30 | K | NIST |
| Tboil | 353.90 ± 0.50 | K | NIST |
| Tboil | 353.90 ± 0.50 | K | NIST |
| Tboil | 353.72 ± 0.30 | K | NIST |
| Tboil | 354.08 ± 0.20 | K | NIST |
| Tboil | 354.15 ± 0.40 | K | NIST |
| Tboil | 353.95 ± 0.25 | K | NIST |
| Tboil | 353.90 ± 0.50 | K | NIST |
| Tboil | 354.00 ± 0.30 | K | NIST |
| Tboil | 353.00 ± 3.00 | K | NIST |
| Tboil | 353.89 ± 0.15 | K | NIST |
| Tboil | 353.80 ± 0.50 | K | NIST |
| Tboil | 353.15 ± 1.00 | K | NIST |
| Tboil | 353.95 ± 0.30 | K | NIST |
| Tboil | 353.81 ± 0.20 | K | NIST |
| Tboil | 352.35 ± 1.50 | K | NIST |
| Tboil | 353.80 ± 0.50 | K | NIST |
| Tboil | 353.80 ± 0.30 | K | NIST |
| Tboil | 353.87 ± 0.15 | K | NIST |
| Tboil | 354.00 ± 0.30 | K | NIST |
| Tboil | 354.00 ± 0.50 | K | NIST |
| Tboil | 353.95 ± 0.30 | K | NIST |
| Tboil | 353.90 ± 0.30 | K | NIST |
| Tboil | 353.80 ± 0.50 | K | NIST |
| Tboil | 353.88 ± 0.01 | K | NIST |
| Tboil | 353.90 ± 1.00 | K | NIST |
| Tboil | 353.70 ± 1.00 | K | NIST |
| Tboil | 354.10 ± 0.40 | K | NIST |
| Tboil | 353.15 ± 0.50 | K | NIST |
| Tboil | 353.89 ± 0.05 | K | NIST |
| Tboil | 353.95 ± 0.30 | K | NIST |
| Tboil | 353.89 ± 0.10 | K | NIST |
| Tboil | 353.75 ± 0.40 | K | NIST |
| Tboil | 353.96 ± 0.10 | K | NIST |
| Tboil | 353.95 ± 0.20 | K | NIST |
| Tboil | 354.10 ± 0.60 | K | NIST |
| Tboil | 354.05 ± 0.40 | K | NIST |
| Tboil | 353.95 ± 0.20 | K | NIST |
| Tboil | 354.40 ± 1.00 | K | NIST |
| Tboil | 353.00 ± 3.00 | K | NIST |
| Tboil | 354.05 ± 0.30 | K | NIST |
| Tboil | 353.95 ± 0.40 | K | NIST |
| Tboil | 354.07 ± 0.30 | K | NIST |
| Tboil | 354.15 ± 1.50 | K | NIST |
| Tboil | 353.65 ± 0.60 | K | NIST |
| Tboil | 353.90 ± 0.30 | K | NIST |
| Tboil | 353.90 ± 0.50 | K | NIST |
| Tboil | 354.15 ± 0.30 | K | NIST |
| Tboil | 353.95 ± 0.10 | K | NIST |
| Tboil | 353.87 ± 0.10 | K | NIST |
| Tboil | 354.00 ± 1.00 | K | NIST |
| Tboil | 354.55 ± 0.30 | K | NIST |
| Tboil | 354.00 ± 0.50 | K | NIST |
| Tboil | 354.55 ± 0.20 | K | NIST |
| Tboil | 356.40 ± 2.00 | K | NIST |
| Tboil | Outlier 356.65 ± 0.50 | K | NIST |
| Tboil | Outlier 342.10 ± 0.20 | K | NIST |
| Tboil | 353.00 ± 2.00 | K | NIST |
| Tboil | 355.00 ± 3.00 | K | NIST |
| Tboil | 354.00 ± 2.00 | K | NIST |
| Tboil | 354.00 ± 1.50 | K | NIST |
| Tboil | Outlier 345.20 ± 8.00 | K | NIST |
| Tboil | Outlier 358.70 ± 3.33 | K | NIST |
| Tc | [552.97; 555.10] | K |
|
| Tc | 553.60 | K | Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC) |
| Tc | 554.10 | K | Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane |
| Tc | 553.61 | K | Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus |
| Tc | 553.60 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tc | 553.80 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Tc | 553.80 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 553.54 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 553.50 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 553.80 | K | KDB |
| Tc | 553.80 ± 0.20 | K | NIST |
| Tc | 553.90 ± 0.40 | K | NIST |
| Tc | 553.70 ± 0.60 | K | NIST |
| Tc | 553.40 | K | NIST |
| Tc | 553.64 ± 0.03 | K | NIST |
| Tc | 553.00 ± 0.30 | K | NIST |
| Tc | Outlier 555.10 ± 0.50 | K | NIST |
| Tc | 553.40 ± 0.60 | K | NIST |
| Tc | 553.35 ± 0.10 | K | NIST |
| Tc | 553.40 ± 0.60 | K | NIST |
| Tc | 553.45 ± 0.15 | K | NIST |
| Tc | 554.15 ± 1.50 | K | NIST |
| Tc | 553.40 ± 0.60 | K | NIST |
| Tc | 552.97 ± 0.10 | K | NIST |
| Tc | 553.90 ± 0.20 | K | NIST |
| Tc | 554.20 ± 1.00 | K | NIST |
| Tc | 553.00 ± 2.00 | K | NIST |
| Tc | 553.20 ± 0.60 | K | NIST |
| Tfus | [266.75; 280.69] | K |
|
| Tfus | 280.10 | K | Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure |
| Tfus | 280.00 | K | Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell |
| Tfus | 279.95 | K | Liquid-Liquid-Solid Equilibria in the Ternary System Water-Phosphoric Acid-Cyclohexane at 25 and 35 deg.C: Stability Domain of Hemihydrate and Anhydrous Phosphoric Acid |
| Tfus | 279.96 | K | Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol |
| Tfus | 280.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 279.69 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 279.70 | K | KDB |
| Tfus | 279.96 | K | Aq. Solubility Prediction |
| Tfus | 280.15 ± 1.00 | K | NIST |
| Tfus | 279.74 ± 0.02 | K | NIST |
| Tfus | 279.66 ± 0.10 | K | NIST |
| Tfus | 279.74 ± 0.08 | K | NIST |
| Tfus | 279.73 ± 0.01 | K | NIST |
| Tfus | 279.87 ± 0.01 | K | NIST |
| Tfus | 279.70 ± 0.05 | K | NIST |
| Tfus | 280.69 ± 0.05 | K | NIST |
| Tfus | 279.73 ± 0.15 | K | NIST |
| Tfus | 279.72 ± 0.04 | K | NIST |
| Tfus | 279.70 ± 0.03 | K | NIST |
| Tfus | 279.58 ± 0.10 | K | NIST |
| Tfus | 279.75 ± 0.30 | K | NIST |
| Tfus | 279.69 ± 0.10 | K | NIST |
| Tfus | 279.22 ± 0.10 | K | NIST |
| Tfus | 279.70 ± 0.20 | K | NIST |
| Tfus | 279.70 ± 0.30 | K | NIST |
| Tfus | 279.65 ± 0.10 | K | NIST |
| Tfus | 279.65 ± 0.30 | K | NIST |
| Tfus | 279.62 ± 0.20 | K | NIST |
| Tfus | 279.55 ± 0.20 | K | NIST |
| Tfus | 279.57 ± 0.06 | K | NIST |
| Tfus | 279.50 ± 0.07 | K | NIST |
| Tfus | 279.69 ± 0.01 | K | NIST |
| Tfus | 279.30 ± 0.80 | K | NIST |
| Tfus | 279.51 ± 0.06 | K | NIST |
| Tfus | 279.65 ± 0.10 | K | NIST |
| Tfus | 279.55 ± 0.20 | K | NIST |
| Tfus | 279.55 ± 0.50 | K | NIST |
| Tfus | 279.55 ± 0.20 | K | NIST |
| Tfus | Outlier 266.75 ± 1.50 | K | NIST |
| Tfus | 277.15 ± 1.00 | K | NIST |
| Tfus | 279.55 ± 0.10 | K | NIST |
| Tfus | 279.00 ± 1.50 | K | NIST |
| Tfus | 279.40 ± 1.00 | K | NIST |
| Tfus | 279.15 ± 0.50 | K | NIST |
| Tfus | 279.35 ± 0.50 | K | NIST |
| Tfus | 279.40 ± 0.60 | K | NIST |
| Tfus | 279.55 ± 0.20 | K | NIST |
| Tfus | 277.70 ± 1.00 | K | NIST |
| Tfus | 279.55 ± 0.40 | K | NIST |
| Tfus | 279.55 ± 0.20 | K | NIST |
| Tfus | 278.65 ± 0.20 | K | NIST |
| Tfus | 279.65 ± 0.50 | K | NIST |
| Tfus | 279.60 ± 2.00 | K | NIST |
| Tfus | 277.90 ± 0.60 | K | NIST |
| Tfus | 278.70 ± 2.77 | K | NIST |
| Ttriple | [186.18; 279.90] | K |
|
| Ttriple | Outlier 186.18 | K | Development of a certified reference material for calibration of DSC and DTA below room temperature: NMIJ CRM 5401-a, Cyclohexane for Thermal Analysis |
| Ttriple | 279.69 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 279.83 | K | KDB |
| Ttriple | 279.70 ± 0.10 | K | NIST |
| Ttriple | 279.83 ± 0.02 | K | NIST |
| Ttriple | 279.90 ± 3.00 | K | NIST |
| Ttriple | 279.84 ± 0.02 | K | NIST |
| Ttriple | 279.82 ± 0.05 | K | NIST |
| Ttriple | 279.40 ± 0.20 | K | NIST |
| Ttriple | 279.78 ± 0.06 | K | NIST |
| Ttriple | 279.30 ± 0.20 | K | NIST |
| UQi | 3.24 | ChemSep v8.3 pure component data Compiled value | |
| URi | 4.05 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.308; 0.309] | m3/kmol |
|
| Vc | 0.308 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Vc | 0.308 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.308 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.308 | m3/kmol | KDB |
| Vc | 0.308 | m3/kmol | NIST |
| Vc | Outlier 0.309 ± 0.003 | m3/kmol | NIST |
| Vm | [1.09e-04; 1.09e-04] | m3/mol |
|
| Vm | 1.09e-04 | m3/mol | Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K |
| Vm | 1.09e-04 | m3/mol | Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies |
| Vm | 1.09e-04 | m3/mol | Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K |
| VCOSTALD | 0.31 | m3/kmol | Hankinson and Thomson (1979), COSTALD parameters Compiled value |
| ωSRK | 0.21 | Hankinson and Thomson (1979), COSTALD parameters Compiled value | |
| Zc | [0.2729110; 0.2730000] |
|
|
| Zc | 0.2730000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value | |
| Zc | 0.2730000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2729110 | 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
Pressure Dependent Properties
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.10 | 2930.00 | 0.0009 |
| 305.20 | 140.00 | 0.0008 |
| 305.10 | 960.00 | 0.0008 |
| 305.20 | 1960.00 | 0.0008 |
| 305.20 | 3940.00 | 0.0008 |
| 313.80 | 2920.00 | 0.0007 |
| 323.70 | 150.00 | 0.0006 |
| 324.00 | 1020.00 | 0.0006 |
| 323.70 | 1990.00 | 0.0006 |
| 323.70 | 4000.00 | 0.0006 |
| 348.90 | 140.00 | 0.0004 |
| 348.90 | 990.00 | 0.0004 |
| 348.90 | 2080.00 | 0.0004 |
| 348.90 | 3030.00 | 0.0005 |
| 348.90 | 3930.00 | 0.0004 |
| 373.70 | 970.00 | 0.0003 |
| 373.70 | 2020.00 | 0.0003 |
| 373.70 | 2930.00 | 0.0003 |
| 373.70 | 3960.00 | 0.0003 |
| 398.20 | 960.00 | 0.0003 |
| 398.10 | 2000.00 | 0.0003 |
| 398.20 | 2940.00 | 0.0003 |
| 398.10 | 4010.00 | 0.0003 |
| 422.40 | 960.00 | 0.0002 |
| 422.50 | 1970.00 | 0.0002 |
| 422.50 | 2960.00 | 0.0002 |
| 422.50 | 3960.00 | 0.0002 |
| 447.50 | 1010.00 | 0.0002 |
| 447.60 | 2040.00 | 0.0002 |
| 447.70 | 3010.00 | 0.0002 |
| 447.70 | 4000.00 | 0.0002 |
| 473.40 | 1930.00 | 0.0001 |
| 473.30 | 3000.00 | 0.0001 |
| 473.40 | 3930.00 | 0.0001 |
| 498.20 | 3020.00 | 0.0001 |
| 497.90 | 3050.00 | 0.0001 |
| 498.10 | 3980.00 | 0.0001 |
| 498.30 | 4020.00 | 0.0001 |
| 523.00 | 3050.00 | 0.0001 |
| 523.00 | 3970.00 | 0.0001 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Viscosity, Pa*s - Liquid |
| 690.00 | 313.20 | 0.0007 |
| 690.00 | 333.20 | 0.0005 |
| 690.00 | 353.20 | 0.0004 |
| 690.00 | 373.20 | 0.0003 |
| 690.00 | 393.20 | 0.0002 |
| 5000.00 | 313.20 | 0.0008 |
| 5000.00 | 333.20 | 0.0006 |
| 5000.00 | 353.20 | 0.0004 |
| 5000.00 | 373.20 | 0.0003 |
| 5000.00 | 393.20 | 0.0003 |
| 10000.00 | 313.20 | 0.0008 |
| 10000.00 | 333.20 | 0.0006 |
| 10000.00 | 353.20 | 0.0005 |
| 10000.00 | 373.20 | 0.0004 |
| 10000.00 | 393.20 | 0.0003 |
| 20000.00 | 313.20 | 0.0009 |
| 20000.00 | 333.20 | 0.0007 |
| 20000.00 | 353.20 | 0.0005 |
| 20000.00 | 373.20 | 0.0004 |
| 20000.00 | 393.20 | 0.0003 |
| 30000.00 | 313.20 | 0.0010 |
| 30000.00 | 333.20 | 0.0008 |
| 30000.00 | 353.20 | 0.0006 |
| 30000.00 | 373.20 | 0.0005 |
| 30000.00 | 393.20 | 0.0004 |
| 40000.00 | 313.20 | 0.0011 |
| 40000.00 | 333.20 | 0.0008 |
| 40000.00 | 353.20 | 0.0007 |
| 40000.00 | 373.20 | 0.0005 |
| 40000.00 | 393.20 | 0.0004 |
| 50000.00 | 313.20 | 0.0012 |
| 50000.00 | 333.20 | 0.0009 |
| 50000.00 | 353.20 | 0.0007 |
| 50000.00 | 373.20 | 0.0006 |
| 50000.00 | 393.20 | 0.0005 |
| 60000.00 | 313.20 | 0.0013 |
| 60000.00 | 333.20 | 0.0010 |
| 60000.00 | 353.20 | 0.0008 |
| 60000.00 | 373.20 | 0.0006 |
| 60000.00 | 393.20 | 0.0005 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 298.15 | 100.00 | 0.0009 |
| 298.15 | 4000.00 | 0.0009 |
| 298.15 | 7600.00 | 0.0010 |
| 298.15 | 13700.00 | 0.0010 |
| 298.15 | 20900.00 | 0.0011 |
| 298.15 | 27700.00 | 0.0012 |
| 298.15 | 34700.00 | 0.0013 |
| 318.15 | 6895.00 | 0.0007 |
| 318.15 | 13790.00 | 0.0007 |
| 318.15 | 20680.00 | 0.0008 |
| 318.15 | 27580.00 | 0.0008 |
| 318.15 | 34470.00 | 0.0009 |
| 318.15 | 41370.00 | 0.0010 |
| 318.15 | 48260.00 | 0.0010 |
| 318.15 | 55160.00 | 0.0011 |
| 318.15 | 62050.00 | 0.0012 |
| 323.15 | 100.00 | 0.0006 |
| 323.15 | 7200.00 | 0.0007 |
| 323.15 | 14200.00 | 0.0007 |
| 323.15 | 21100.00 | 0.0008 |
| 323.15 | 27700.00 | 0.0008 |
| 323.15 | 40000.00 | 0.0010 |
| 323.15 | 48200.00 | 0.0010 |
| 323.15 | 50900.00 | 0.0011 |
| 323.15 | 52300.00 | 0.0011 |
| 323.15 | 54300.00 | 0.0011 |
| 323.15 | 55000.00 | 0.0009 |
| 333.15 | 100.00 | 0.0005 |
| 333.15 | 3800.00 | 0.0005 |
| 333.15 | 6895.00 | 0.0005 |
| 333.15 | 7300.00 | 0.0006 |
| 333.15 | 13790.00 | 0.0006 |
| 333.15 | 14100.00 | 0.0006 |
| 333.15 | 20600.00 | 0.0007 |
| 333.15 | 20680.00 | 0.0006 |
| 333.15 | 27580.00 | 0.0007 |
| 333.15 | 27800.00 | 0.0007 |
| 333.15 | 34470.00 | 0.0008 |
| 333.15 | 34700.00 | 0.0008 |
| 333.15 | 41370.00 | 0.0008 |
| 333.15 | 42000.00 | 0.0008 |
| 333.15 | 48260.00 | 0.0009 |
| 333.15 | 49000.00 | 0.0009 |
| 333.15 | 53500.00 | 0.0009 |
| 333.15 | 55160.00 | 0.0009 |
| 333.15 | 62050.00 | 0.0010 |
| 348.15 | 6895.00 | 0.0005 |
| 348.15 | 13790.00 | 0.0005 |
| 348.15 | 20680.00 | 0.0005 |
| 348.15 | 27580.00 | 0.0006 |
| 348.15 | 34470.00 | 0.0006 |
| 348.15 | 41370.00 | 0.0007 |
| 348.15 | 48260.00 | 0.0007 |
| 348.15 | 55160.00 | 0.0008 |
| 348.15 | 62050.00 | 0.0008 |
| 363.15 | 6895.00 | 0.0004 |
| 363.15 | 13790.00 | 0.0004 |
| 363.15 | 20680.00 | 0.0005 |
| 363.15 | 27580.00 | 0.0005 |
| 363.15 | 34470.00 | 0.0005 |
| 363.15 | 41370.00 | 0.0006 |
| 363.15 | 48260.00 | 0.0006 |
| 363.15 | 55160.00 | 0.0007 |
| 363.15 | 62050.00 | 0.0007 |
| 388.15 | 6895.00 | 0.0003 |
| 388.15 | 13790.00 | 0.0003 |
| 388.15 | 20680.00 | 0.0004 |
| 388.15 | 27580.00 | 0.0004 |
| 388.15 | 34470.00 | 0.0004 |
| 388.15 | 41370.00 | 0.0004 |
| 388.15 | 48260.00 | 0.0005 |
| 388.15 | 55160.00 | 0.0005 |
| 388.15 | 62050.00 | 0.0005 |
| 413.15 | 6895.00 | 0.0002 |
| 413.15 | 13790.00 | 0.0003 |
| 413.15 | 20680.00 | 0.0003 |
| 413.15 | 27580.00 | 0.0003 |
| 413.15 | 34470.00 | 0.0003 |
| 413.15 | 41370.00 | 0.0004 |
| 413.15 | 48260.00 | 0.0004 |
| 413.15 | 55160.00 | 0.0004 |
| 413.15 | 62050.00 | 0.0004 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 773.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 99.46 | 778.632 |
| 293.15 | 1102.03 | 779.471 |
| 293.15 | 2002.37 | 780.22 |
| 293.15 | 4003.86 | 781.856 |
| 293.15 | 6003.84 | 783.454 |
| 293.15 | 8003.30 | 785.025 |
| 293.15 | 10042.20 | 786.595 |
| 293.15 | 12045.50 | 788.105 |
| 293.15 | 13918.70 | 789.495 |
| 293.15 | 15982.40 | 790.995 |
| 293.15 | 17946.40 | 792.401 |
| 293.15 | 20017.10 | 793.855 |
| 313.15 | 102.48 | 759.667 |
| 313.15 | 1139.02 | 760.675 |
| 313.15 | 2012.18 | 761.509 |
| 313.15 | 4102.38 | 763.47 |
| 313.15 | 5932.83 | 765.157 |
| 313.15 | 7910.50 | 766.936 |
| 313.15 | 10017.50 | 768.784 |
| 313.15 | 12069.20 | 770.545 |
| 313.15 | 13964.70 | 772.137 |
| 313.15 | 15901.80 | 773.737 |
| 313.15 | 17955.80 | 775.394 |
| 313.15 | 20142.40 | 777.123 |
| 333.15 | 1112.41 | 741.367 |
| 333.15 | 2043.58 | 742.401 |
| 333.15 | 3987.96 | 744.517 |
| 333.15 | 5966.83 | 746.613 |
| 333.15 | 8141.84 | 748.853 |
| 333.15 | 10007.20 | 750.72 |
| 333.15 | 11993.60 | 752.664 |
| 333.15 | 14092.70 | 754.666 |
| 333.15 | 15962.90 | 756.414 |
| 333.15 | 17994.70 | 758.261 |
| 333.15 | 19860.60 | 759.929 |
| 353.15 | 1109.91 | 721.547 |
| 353.15 | 1973.18 | 722.669 |
| 353.15 | 4000.02 | 725.242 |
| 353.15 | 6001.27 | 727.698 |
| 353.15 | 8046.51 | 730.125 |
| 353.15 | 10046.10 | 732.423 |
| 353.15 | 11820.50 | 734.413 |
| 353.15 | 13860.00 | 736.633 |
| 353.15 | 15939.70 | 738.835 |
| 353.15 | 18023.40 | 740.978 |
| 353.15 | 20002.80 | 742.965 |
| 373.15 | 1115.51 | 701.065 |
| 373.15 | 1950.06 | 702.346 |
| 373.15 | 4154.07 | 705.638 |
| 373.15 | 6126.03 | 708.455 |
| 373.15 | 8029.39 | 711.079 |
| 373.15 | 9951.24 | 713.63 |
| 373.15 | 12097.10 | 716.383 |
| 373.15 | 13877.00 | 718.592 |
| 373.15 | 16148.10 | 721.319 |
| 373.15 | 18077.70 | 723.568 |
| 373.15 | 19877.00 | 725.607 |
| 393.15 | 1162.91 | 679.792 |
| 393.15 | 1960.31 | 681.265 |
| 393.15 | 3901.42 | 684.723 |
| 393.15 | 5983.91 | 688.253 |
| 393.15 | 7986.39 | 691.487 |
| 393.15 | 9903.28 | 694.452 |
| 393.15 | 11974.70 | 697.527 |
| 393.15 | 13821.00 | 700.163 |
| 393.15 | 16029.30 | 703.195 |
| 393.15 | 18027.30 | 705.845 |
| 393.15 | 20003.70 | 708.371 |
| 413.15 | 1196.72 | 657.32 |
| 413.15 | 2172.63 | 659.527 |
| 413.15 | 4146.43 | 663.767 |
| 413.15 | 6122.26 | 667.756 |
| 413.15 | 8132.63 | 671.583 |
| 413.15 | 10013.20 | 674.989 |
| 413.15 | 11993.30 | 678.397 |
| 413.15 | 14003.50 | 681.703 |
| 413.15 | 16052.90 | 684.936 |
| 413.15 | 18098.20 | 688.022 |
| 413.15 | 19934.80 | 690.694 |
| 433.15 | 1086.72 | 632.817 |
| 433.15 | 2070.58 | 635.63 |
| 433.15 | 4050.34 | 640.931 |
| 433.15 | 6077.00 | 645.937 |
| 433.15 | 8181.71 | 650.742 |
| 433.15 | 10076.70 | 654.811 |
| 433.15 | 12111.10 | 658.913 |
| 433.15 | 13890.30 | 662.325 |
| 433.15 | 15958.80 | 666.096 |
| 433.15 | 18073.30 | 669.76 |
| 433.15 | 20009.80 | 672.969 |
| 453.15 | 2100.81 | 609.942 |
| 453.15 | 4117.30 | 616.844 |
| 453.15 | 6121.33 | 623.004 |
| 453.15 | 8117.44 | 628.596 |
| 453.15 | 9915.40 | 633.254 |
| 453.15 | 11931.40 | 638.115 |
| 453.15 | 13934.70 | 642.628 |
| 453.15 | 15959.00 | 646.918 |
| 453.15 | 18103.10 | 651.206 |
| 453.15 | 19890.50 | 654.601 |
| 473.15 | 2403.47 | 582.448 |
| 473.15 | 3924.93 | 589.431 |
| 473.15 | 6045.23 | 597.933 |
| 473.15 | 8093.25 | 605.148 |
| 473.15 | 9884.30 | 610.832 |
| 473.15 | 11911.40 | 616.733 |
| 473.15 | 13942.60 | 622.171 |
| 473.15 | 16018.50 | 627.319 |
| 473.15 | 18132.60 | 632.216 |
| 473.15 | 20025.00 | 636.335 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 288.15 | 100.00 | 782.7 |
| 288.15 | 1000.00 | 783.7 |
| 288.15 | 5000.00 | 787.0 |
| 288.15 | 10000.00 | 790.7 |
| 288.15 | 15000.00 | 794.1 |
| 298.15 | 100.00 | 773.2 |
| 298.15 | 1000.00 | 774.0 |
| 298.15 | 5000.00 | 777.6 |
| 298.15 | 10000.00 | 781.8 |
| 298.15 | 15000.00 | 785.6 |
| 298.15 | 20000.00 | 789.3 |
| 298.15 | 25000.00 | 792.9 |
| 298.15 | 30000.00 | 796.8 |
| 298.15 | 35000.00 | 799.7 |
| 308.15 | 100.00 | 763.6 |
| 308.15 | 1000.00 | 764.5 |
| 308.15 | 5000.00 | 768.2 |
| 308.15 | 10000.00 | 772.6 |
| 308.15 | 15000.00 | 776.8 |
| 308.15 | 20000.00 | 780.8 |
| 308.15 | 25000.00 | 784.6 |
| 308.15 | 30000.00 | 788.3 |
| 308.15 | 35000.00 | 791.8 |
| 308.15 | 40000.00 | 795.2 |
| 318.15 | 100.00 | 754.0 |
| 318.15 | 1000.00 | 755.0 |
| 318.15 | 5000.00 | 759.0 |
| 318.15 | 10000.00 | 763.7 |
| 318.15 | 15000.00 | 767.9 |
| 318.15 | 20000.00 | 772.4 |
| 318.15 | 25000.00 | 776.4 |
| 318.15 | 30000.00 | 780.3 |
| 318.15 | 35000.00 | 784.1 |
| 318.15 | 40000.00 | 787.7 |
| 318.15 | 45000.00 | 791.1 |
| 318.15 | 50000.00 | 794.4 |
| 328.15 | 100.00 | 744.4 |
| 328.15 | 1000.00 | 745.4 |
| 328.15 | 5000.00 | 749.7 |
| 328.15 | 10000.00 | 754.7 |
| 328.15 | 15000.00 | 759.5 |
| 328.15 | 20000.00 | 764.0 |
| 328.15 | 25000.00 | 768.2 |
| 328.15 | 30000.00 | 772.3 |
| 328.15 | 35000.00 | 776.1 |
| 328.15 | 40000.00 | 779.9 |
| 328.15 | 45000.00 | 783.5 |
| 328.15 | 50000.00 | 787.0 |
| 338.15 | 100.00 | 734.5 |
| 338.15 | 1000.00 | 735.6 |
| 338.15 | 5000.00 | 740.2 |
| 338.15 | 10000.00 | 745.7 |
| 338.15 | 15000.00 | 750.7 |
| 338.15 | 20000.00 | 755.5 |
| 338.15 | 25000.00 | 760.0 |
| 338.15 | 30000.00 | 764.3 |
| 338.15 | 35000.00 | 768.4 |
| 338.15 | 40000.00 | 772.3 |
| 338.15 | 45000.00 | 776.0 |
| 338.15 | 50000.00 | 779.7 |
| 338.15 | 55000.00 | 783.2 |
| 348.15 | 100.00 | 724.6 |
| 348.15 | 1000.00 | 725.7 |
| 348.15 | 5000.00 | 730.8 |
| 348.15 | 10000.00 | 736.5 |
| 348.15 | 15000.00 | 741.9 |
| 348.15 | 20000.00 | 747.0 |
| 348.15 | 25000.00 | 751.7 |
| 348.15 | 30000.00 | 756.2 |
| 348.15 | 35000.00 | 760.5 |
| 348.15 | 40000.00 | 764.6 |
| 348.15 | 45000.00 | 768.6 |
| 348.15 | 50000.00 | 772.3 |
| 348.15 | 55000.00 | 776.0 |
| 358.15 | 100.00 | 714.3 |
| 358.15 | 1000.00 | 715.6 |
| 358.15 | 5000.00 | 720.9 |
| 358.15 | 10000.00 | 727.2 |
| 358.15 | 15000.00 | 732.9 |
| 358.15 | 20000.00 | 738.3 |
| 358.15 | 25000.00 | 743.3 |
| 358.15 | 30000.00 | 748.1 |
| 358.15 | 35000.00 | 752.6 |
| 358.15 | 40000.00 | 757.0 |
| 358.15 | 45000.00 | 761.1 |
| 358.15 | 50000.00 | 765.0 |
| 358.15 | 55000.00 | 768.9 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 788.0 |
| 283.15 | 1000.00 | 788.7 |
| 283.15 | 2000.00 | 789.5 |
| 283.15 | 5000.00 | 791.8 |
| 293.15 | 100.00 | 778.8 |
| 293.15 | 1000.00 | 779.5 |
| 293.15 | 2000.00 | 780.4 |
| 293.15 | 5000.00 | 782.8 |
| 293.15 | 10000.00 | 786.6 |
| 293.15 | 15000.00 | 790.4 |
| 293.15 | 20000.00 | 793.9 |
| 313.15 | 100.00 | 759.8 |
| 313.15 | 1000.00 | 760.6 |
| 313.15 | 2000.00 | 761.5 |
| 313.15 | 5000.00 | 764.4 |
| 313.15 | 10000.00 | 768.7 |
| 313.15 | 15000.00 | 772.9 |
| 313.15 | 20000.00 | 776.9 |
| 333.15 | 100.00 | 740.5 |
| 333.15 | 1000.00 | 741.5 |
| 333.15 | 2000.00 | 742.6 |
| 333.15 | 5000.00 | 745.8 |
| 333.15 | 10000.00 | 750.9 |
| 333.15 | 15000.00 | 755.6 |
| 333.15 | 20000.00 | 760.1 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.15 | 100.00 | 778.4 |
| 293.15 | 1000.00 | 779.1 |
| 293.15 | 2000.00 | 779.9 |
| 293.15 | 5000.00 | 782.4 |
| 293.15 | 10000.00 | 786.3 |
| 293.15 | 15000.00 | 789.9 |
| 293.15 | 20000.00 | 793.4 |
| 303.15 | 100.00 | 769.0 |
| 303.15 | 1000.00 | 769.8 |
| 303.15 | 2000.00 | 770.7 |
| 303.15 | 5000.00 | 773.3 |
| 303.15 | 10000.00 | 777.5 |
| 303.15 | 15000.00 | 781.3 |
| 303.15 | 20000.00 | 785.1 |
| 303.15 | 30000.00 | 792.1 |
| 303.15 | 40000.00 | 798.5 |
| 313.15 | 100.00 | 759.7 |
| 313.15 | 1000.00 | 760.3 |
| 313.15 | 2000.00 | 761.2 |
| 313.15 | 5000.00 | 764.0 |
| 313.15 | 10000.00 | 768.4 |
| 313.15 | 15000.00 | 772.6 |
| 313.15 | 20000.00 | 776.6 |
| 313.15 | 30000.00 | 784.1 |
| 313.15 | 40000.00 | 790.9 |
| 323.15 | 100.00 | 750.1 |
| 323.15 | 1000.00 | 750.8 |
| 323.15 | 2000.00 | 751.8 |
| 323.15 | 5000.00 | 754.8 |
| 323.15 | 10000.00 | 759.5 |
| 323.15 | 15000.00 | 763.9 |
| 323.15 | 20000.00 | 768.2 |
| 323.15 | 30000.00 | 776.1 |
| 323.15 | 40000.00 | 783.2 |
| 333.15 | 100.00 | 740.3 |
| 333.15 | 1000.00 | 741.1 |
| 333.15 | 2000.00 | 742.2 |
| 333.15 | 5000.00 | 745.5 |
| 333.15 | 10000.00 | 750.5 |
| 333.15 | 15000.00 | 755.3 |
| 333.15 | 20000.00 | 759.7 |
| 333.15 | 30000.00 | 768.1 |
| 333.15 | 40000.00 | 775.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 318.15 | 6895.00 | 761.5 |
| 318.15 | 13789.00 | 767.7 |
| 318.15 | 20684.00 | 773.8 |
| 318.15 | 27579.00 | 779.0 |
| 318.15 | 34474.00 | 784.1 |
| 318.15 | 41369.00 | 788.7 |
| 318.15 | 48263.00 | 793.4 |
| 318.15 | 55158.00 | 797.4 |
| 318.15 | 62053.00 | 801.4 |
| 333.15 | 6895.00 | 747.3 |
| 333.15 | 13789.00 | 754.1 |
| 333.15 | 20684.00 | 760.5 |
| 333.15 | 27579.00 | 766.5 |
| 333.15 | 34474.00 | 772.0 |
| 333.15 | 41369.00 | 777.0 |
| 333.15 | 48263.00 | 781.7 |
| 333.15 | 55158.00 | 786.3 |
| 333.15 | 62053.00 | 790.7 |
| 348.15 | 6895.00 | 733.6 |
| 348.15 | 13789.00 | 741.2 |
| 348.15 | 20684.00 | 748.2 |
| 348.15 | 27579.00 | 754.5 |
| 348.15 | 34474.00 | 760.5 |
| 348.15 | 41369.00 | 766.1 |
| 348.15 | 48263.00 | 771.4 |
| 348.15 | 55158.00 | 776.2 |
| 348.15 | 62053.00 | 781.1 |
| 363.15 | 6895.00 | 719.6 |
| 363.15 | 13789.00 | 727.9 |
| 363.15 | 20684.00 | 735.7 |
| 363.15 | 27579.00 | 742.8 |
| 363.15 | 34474.00 | 749.1 |
| 363.15 | 41369.00 | 755.3 |
| 363.15 | 48263.00 | 760.7 |
| 363.15 | 55158.00 | 765.8 |
| 363.15 | 62053.00 | 771.0 |
| 388.15 | 6895.00 | 694.7 |
| 388.15 | 13789.00 | 705.0 |
| 388.15 | 20684.00 | 713.9 |
| 388.15 | 27579.00 | 721.9 |
| 388.15 | 34474.00 | 729.2 |
| 388.15 | 41369.00 | 736.0 |
| 388.15 | 48263.00 | 742.2 |
| 388.15 | 55158.00 | 747.8 |
| 388.15 | 62053.00 | 753.2 |
| 413.15 | 6895.00 | 669.7 |
| 413.15 | 13789.00 | 682.1 |
| 413.15 | 20684.00 | 692.5 |
| 413.15 | 27579.00 | 701.8 |
| 413.15 | 34474.00 | 710.1 |
| 413.15 | 41369.00 | 717.7 |
| 413.15 | 48263.00 | 724.9 |
| 413.15 | 55158.00 | 731.2 |
| 413.15 | 62053.00 | 737.2 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [43.78; 363.77] | J/mol×K | [100.00; 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 | 4.25690e+01 | |||
| Coefficient B | -5.88900e+02 | |||
| Coefficient C | 6.05424e+00 | |||
| Coefficient D | 2.83760e-04 | |||
| Coefficient E | -1.40090e-07 | |||
| Temperature range, min. | 100.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 43.78 | J/mol×K | 100.00 | Calculated Property |
| Cp,gas | 87.87 | J/mol×K | 255.56 | Calculated Property |
| Cp,gas | 154.15 | J/mol×K | 411.11 | Calculated Property |
| Cp,gas | 211.73 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 257.58 | J/mol×K | 722.22 | Calculated Property |
| Cp,gas | 293.33 | J/mol×K | 877.78 | Calculated Property |
| Cp,gas | 320.67 | J/mol×K | 1033.33 | Calculated Property |
| Cp,gas | 340.92 | J/mol×K | 1188.89 | Calculated Property |
| Cp,gas | 355.04 | J/mol×K | 1344.44 | Calculated Property |
| Cp,gas | 363.77 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [149.60; 202.65] | J/mol×K | [279.69; 400.00] |
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 | 1.16110e+02 | |||
| Coefficient B | 1.27670e+02 | |||
| Coefficient C | -1.42355e-01 | |||
| Coefficient D | 1.31100e-02 | |||
| Coefficient E | -6.00130e-06 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 400.00 | |||
| Cp,liquid | 149.60 | J/mol×K | 279.69 | Calculated Property |
| Cp,liquid | 153.44 | J/mol×K | 293.06 | Calculated Property |
| Cp,liquid | 157.71 | J/mol×K | 306.43 | Calculated Property |
| Cp,liquid | 162.43 | J/mol×K | 319.79 | Calculated Property |
| Cp,liquid | 167.66 | J/mol×K | 333.16 | Calculated Property |
| Cp,liquid | 173.42 | J/mol×K | 346.53 | Calculated Property |
| Cp,liquid | 179.75 | J/mol×K | 359.90 | Calculated Property |
| Cp,liquid | 186.71 | J/mol×K | 373.26 | Calculated Property |
| Cp,liquid | 194.33 | J/mol×K | 386.63 | Calculated Property |
| Cp,liquid | 202.65 | J/mol×K | 400.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0012622; 0.0000616] | Pa×s | [279.69; 553.50] |
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 | -1.32285e+02 | |||
| Coefficient B | 5.90541e+03 | |||
| Coefficient C | 1.88809e+01 | |||
| Coefficient D | -2.39420e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 553.50 | |||
| η | 0.0012622 | Pa×s | 279.69 | Calculated Property |
| η | 0.0007272 | Pa×s | 310.11 | Calculated Property |
| η | 0.0004835 | Pa×s | 340.54 | Calculated Property |
| η | 0.0003494 | Pa×s | 370.96 | Calculated Property |
| η | 0.0002638 | Pa×s | 401.38 | Calculated Property |
| η | 0.0002026 | Pa×s | 431.81 | Calculated Property |
| η | 0.0001553 | Pa×s | 462.23 | Calculated Property |
| η | 0.0001173 | Pa×s | 492.65 | Calculated Property |
| η | 0.0000864 | Pa×s | 523.08 | Calculated Property |
| η | 0.0000616 | Pa×s | 553.50 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [34.15; 9.20] | kJ/mol | [273.15; 543.15] |
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 | 4.48560e+01 | |||
| Coefficient B | 3.56910e-01 | |||
| Coefficient C | 2.61810e-01 | |||
| Coefficient D | -4.76470e-01 | |||
| Coefficient E | 2.57410e-01 | |||
| Critical temperature, Tc (K) | 5.53500e+02 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 543.15 | |||
| ΔvapH | 34.15 | kJ/mol | 273.15 | Calculated Property |
| ΔvapH | 32.67 | kJ/mol | 303.15 | Calculated Property |
| ΔvapH | 31.09 | kJ/mol | 333.15 | Calculated Property |
| ΔvapH | 29.38 | kJ/mol | 363.15 | Calculated Property |
| ΔvapH | 27.51 | kJ/mol | 393.15 | Calculated Property |
| ΔvapH | 25.39 | kJ/mol | 423.15 | Calculated Property |
| ΔvapH | 22.92 | kJ/mol | 453.15 | Calculated Property |
| ΔvapH | 19.92 | kJ/mol | 483.15 | Calculated Property |
| ΔvapH | 15.93 | kJ/mol | 513.15 | Calculated Property |
| ΔvapH | 9.20 | kJ/mol | 543.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [258.23; 378.22] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.38484e+01 | |||
| Coefficient B | -2.76500e+03 | |||
| Coefficient C | -5.43350e+01 | |||
| Temperature range, min. | 258.23 | |||
| Temperature range, max. | 378.22 | |||
| Pvap | 1.33 | kPa | 258.23 | Calculated Property |
| Pvap | 3.06 | kPa | 271.56 | Calculated Property |
| Pvap | 6.40 | kPa | 284.89 | Calculated Property |
| Pvap | 12.32 | kPa | 298.23 | Calculated Property |
| Pvap | 22.18 | kPa | 311.56 | Calculated Property |
| Pvap | 37.66 | kPa | 324.89 | Calculated Property |
| Pvap | 60.86 | kPa | 338.22 | Calculated Property |
| Pvap | 94.21 | kPa | 351.56 | Calculated Property |
| Pvap | 140.46 | kPa | 364.89 | Calculated Property |
| Pvap | 202.64 | kPa | 378.22 | Calculated Property |
| Pvap | [2.09; 4069.79] | kPa | [263.06; 553.50] |
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 | 7.29219e+01 | |||
| Coefficient B | -6.24669e+03 | |||
| Coefficient C | -8.77877e+00 | |||
| Coefficient D | 6.93373e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 553.8 K. | |||
| Temperature range, min. | 263.06 | |||
| Temperature range, max. | 553.50 | |||
| Pvap | 2.09 | kPa | 263.06 | Calculated Property |
| Pvap | 11.48 | kPa | 295.33 | Calculated Property |
| Pvap | 42.66 | kPa | 327.60 | Calculated Property |
| Pvap | 120.57 | kPa | 359.87 | Calculated Property |
| Pvap | 280.07 | kPa | 392.14 | Calculated Property |
| Pvap | 563.82 | kPa | 424.42 | Calculated Property |
| Pvap | 1021.05 | kPa | 456.69 | Calculated Property |
| Pvap | 1708.80 | kPa | 488.96 | Calculated Property |
| Pvap | 2695.90 | kPa | 521.23 | Calculated Property |
| Pvap | 4069.79 | kPa | 553.50 | Calculated Property |
| Pvap | [5.32; 4077.96] | kPa | [279.69; 553.54] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 7.56506e+01 | |||
| Coefficient B | -6.35490e+03 | |||
| Coefficient C | -9.20098e+00 | |||
| Coefficient D | 7.37481e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 553.54 | |||
| Pvap | 5.32 | kPa | 279.69 | Calculated Property |
| Pvap | 21.81 | kPa | 310.12 | Calculated Property |
| Pvap | 66.56 | kPa | 340.55 | Calculated Property |
| Pvap | 164.18 | kPa | 370.97 | Calculated Property |
| Pvap | 346.38 | kPa | 401.40 | Calculated Property |
| Pvap | 650.51 | kPa | 431.83 | Calculated Property |
| Pvap | 1119.43 | kPa | 462.26 | Calculated Property |
| Pvap | 1803.27 | kPa | 492.68 | Calculated Property |
| Pvap | 2763.29 | kPa | 523.11 | Calculated Property |
| Pvap | 4077.96 | kPa | 553.54 | Calculated Property |
| Pvap | [36.24; 2746.36] | kPa | [323.00; 523.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41375e+01 | |||
| Coefficient B | -3.03148e+03 | |||
| Coefficient C | -3.55810e+01 | |||
| Reference | Kerns, Anthony, et al., 1974 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 323.00 | |||
| Temperature range, max. | 523.00 | |||
| Pvap | 36.24 | kPa | 323.00 | Calculated Property |
| Pvap | 77.26 | kPa | 345.22 | Calculated Property |
| Pvap | 148.82 | kPa | 367.44 | Calculated Property |
| Pvap | 264.03 | kPa | 389.67 | Calculated Property |
| Pvap | 437.75 | kPa | 411.89 | Calculated Property |
| Pvap | 685.97 | kPa | 434.11 | Calculated Property |
| Pvap | 1025.14 | kPa | 456.33 | Calculated Property |
| Pvap | 1471.48 | kPa | 478.56 | Calculated Property |
| Pvap | 2040.46 | kPa | 500.78 | Calculated Property |
| Pvap | 2746.36 | kPa | 523.00 | Calculated Property |
| Pvap | [16.15; 72.13] | kPa | [303.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37971e+01 | |||
| Coefficient B | -2.80208e+03 | |||
| Coefficient C | -4.86210e+01 | |||
| Reference | Gaw and Swinton, 1968, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 303.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 16.15 | kPa | 303.00 | Calculated Property |
| Pvap | 19.51 | kPa | 307.44 | Calculated Property |
| Pvap | 23.42 | kPa | 311.89 | Calculated Property |
| Pvap | 27.95 | kPa | 316.33 | Calculated Property |
| Pvap | 33.16 | kPa | 320.78 | Calculated Property |
| Pvap | 39.12 | kPa | 325.22 | Calculated Property |
| Pvap | 45.92 | kPa | 329.67 | Calculated Property |
| Pvap | 53.63 | kPa | 334.11 | Calculated Property |
| Pvap | 62.34 | kPa | 338.56 | Calculated Property |
| Pvap | 72.13 | kPa | 343.00 | Calculated Property |
| Pvap | [26.64; 101.34] | kPa | [315.70; 353.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.19072e+01 | |||
| Coefficient B | -1.79748e+03 | |||
| Coefficient C | -1.07290e+02 | |||
| Reference | Marinichev and Susarev, 1965, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 315.70 | |||
| Temperature range, max. | 353.90 | |||
| Pvap | 26.64 | kPa | 315.70 | Calculated Property |
| Pvap | 31.65 | kPa | 319.94 | Calculated Property |
| Pvap | 37.34 | kPa | 324.19 | Calculated Property |
| Pvap | 43.78 | kPa | 328.43 | Calculated Property |
| Pvap | 51.02 | kPa | 332.68 | Calculated Property |
| Pvap | 59.12 | kPa | 336.92 | Calculated Property |
| Pvap | 68.15 | kPa | 341.17 | Calculated Property |
| Pvap | 78.15 | kPa | 345.41 | Calculated Property |
| Pvap | 89.20 | kPa | 349.66 | Calculated Property |
| Pvap | 101.34 | kPa | 353.90 | Calculated Property |
| Pvap | [10.29; 103.91] | kPa | [293.06; 354.73] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37462e+01 | |||
| Coefficient B | -2.77122e+03 | |||
| Coefficient C | -5.02870e+01 | |||
| Reference | Williamham, Taylor, et al., 1945 | |||
| Temperature range, min. | 293.06 | |||
| Temperature range, max. | 354.73 | |||
| Pvap | 10.29 | kPa | 293.06 | Calculated Property |
| Pvap | 14.08 | kPa | 299.91 | Calculated Property |
| Pvap | 18.94 | kPa | 306.76 | Calculated Property |
| Pvap | 25.09 | kPa | 313.62 | Calculated Property |
| Pvap | 32.76 | kPa | 320.47 | Calculated Property |
| Pvap | 42.22 | kPa | 327.32 | Calculated Property |
| Pvap | 53.75 | kPa | 334.17 | Calculated Property |
| Pvap | 67.66 | kPa | 341.03 | Calculated Property |
| Pvap | 84.27 | kPa | 347.88 | Calculated Property |
| Pvap | 103.91 | kPa | 354.73 | Calculated Property |
| Pvap | [16.15; 72.13] | kPa | [303.00; 343.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37971e+01 | |||
| Coefficient B | -2.80208e+03 | |||
| Coefficient C | -4.86210e+01 | |||
| Reference | Gaw and Swinton, 1968 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 303.00 | |||
| Temperature range, max. | 343.00 | |||
| Pvap | 16.15 | kPa | 303.00 | Calculated Property |
| Pvap | 19.51 | kPa | 307.44 | Calculated Property |
| Pvap | 23.42 | kPa | 311.89 | Calculated Property |
| Pvap | 27.95 | kPa | 316.33 | Calculated Property |
| Pvap | 33.16 | kPa | 320.78 | Calculated Property |
| Pvap | 39.12 | kPa | 325.22 | Calculated Property |
| Pvap | 45.92 | kPa | 329.67 | Calculated Property |
| Pvap | 53.63 | kPa | 334.11 | Calculated Property |
| Pvap | 62.34 | kPa | 338.56 | Calculated Property |
| Pvap | 72.13 | kPa | 343.00 | Calculated Property |
| Pvap | [26.64; 101.34] | kPa | [315.70; 353.90] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.19072e+01 | |||
| Coefficient B | -1.79748e+03 | |||
| Coefficient C | -1.07290e+02 | |||
| Reference | Marinichev and Susarev, 1965 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 315.70 | |||
| Temperature range, max. | 353.90 | |||
| Pvap | 26.64 | kPa | 315.70 | Calculated Property |
| Pvap | 31.65 | kPa | 319.94 | Calculated Property |
| Pvap | 37.34 | kPa | 324.19 | Calculated Property |
| Pvap | 43.78 | kPa | 328.43 | Calculated Property |
| Pvap | 51.02 | kPa | 332.68 | Calculated Property |
| Pvap | 59.12 | kPa | 336.92 | Calculated Property |
| Pvap | 68.15 | kPa | 341.17 | Calculated Property |
| Pvap | 78.15 | kPa | 345.41 | Calculated Property |
| Pvap | 89.20 | kPa | 349.66 | Calculated Property |
| Pvap | 101.34 | kPa | 353.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [789.63; 432.61] | kg/m3 | [279.69; 539.37] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 7.86546e+01 | |||
| Coefficient B | 2.80220e-01 | |||
| Coefficient C | 5.53500e+02 | |||
| Coefficient D | 2.94090e-01 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 539.37 | |||
| ρl | 789.63 | kg/m3 | 279.69 | Calculated Property |
| ρl | 763.75 | kg/m3 | 308.54 | Calculated Property |
| ρl | 736.58 | kg/m3 | 337.40 | Calculated Property |
| ρl | 707.83 | kg/m3 | 366.25 | Calculated Property |
| ρl | 677.08 | kg/m3 | 395.10 | Calculated Property |
| ρl | 643.69 | kg/m3 | 423.96 | Calculated Property |
| ρl | 606.64 | kg/m3 | 452.81 | Calculated Property |
| ρl | 564.02 | kg/m3 | 481.66 | Calculated Property |
| ρl | 511.46 | kg/m3 | 510.52 | Calculated Property |
| ρl | 432.61 | kg/m3 | 539.37 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [279.75; 353.85] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 6.00702e-02 | |||
| Coefficient B | -1.18800e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 279.75 | |||
| Temperature range, max. | 353.85 | |||
| γ | 0.03 | N/m | 279.75 | Calculated Property |
| γ | 0.03 | N/m | 287.98 | Calculated Property |
| γ | 0.02 | N/m | 296.22 | Calculated Property |
| γ | 0.02 | N/m | 304.45 | Calculated Property |
| γ | 0.02 | N/m | 312.68 | Calculated Property |
| γ | 0.02 | N/m | 320.92 | Calculated Property |
| γ | 0.02 | N/m | 329.15 | Calculated Property |
| γ | 0.02 | N/m | 337.38 | Calculated Property |
| γ | 0.02 | N/m | 345.62 | Calculated Property |
| γ | 0.02 | N/m | 353.85 | Calculated Property |
| γ | [0.03; 5.56e-04] | N/m | [273.15; 539.37] |
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 | -8.74820e-03 | |||
| Coefficient B | 7.63180e+01 | |||
| Coefficient C | -3.60170e+00 | |||
| Coefficient D | 2.38680e-03 | |||
| Coefficient E | -8.60880e-06 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 539.37 | |||
| γ | 0.03 | N/m | 273.15 | Calculated Property |
| γ | 0.02 | N/m | 302.73 | Calculated Property |
| γ | 0.02 | N/m | 332.31 | Calculated Property |
| γ | 0.02 | N/m | 361.89 | Calculated Property |
| γ | 0.01 | N/m | 391.47 | Calculated Property |
| γ | 0.01 | N/m | 421.05 | Calculated Property |
| γ | 0.01 | N/m | 450.63 | Calculated Property |
| γ | 0.01 | N/m | 480.21 | Calculated Property |
| γ | 0.00 | N/m | 509.79 | Calculated Property |
| γ | 5.56e-04 | N/m | 539.37 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.14] | W/m×K | [279.69; 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 | 8.58650e-07 | |||
| Coefficient B | 1.77100e+00 | |||
| Coefficient C | 2.43160e+02 | |||
| Coefficient D | -9.17790e+00 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 279.69 | Calculated Property |
| λgas | 0.02 | W/m×K | 359.72 | Calculated Property |
| λgas | 0.03 | W/m×K | 439.76 | Calculated Property |
| λgas | 0.04 | W/m×K | 519.79 | Calculated Property |
| λgas | 0.05 | W/m×K | 599.83 | Calculated Property |
| λgas | 0.07 | W/m×K | 679.86 | Calculated Property |
| λgas | 0.08 | W/m×K | 759.90 | Calculated Property |
| λgas | 0.10 | W/m×K | 839.93 | Calculated Property |
| λgas | 0.12 | W/m×K | 919.97 | Calculated Property |
| λgas | 0.14 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.13; 0.11] | W/m×K | [279.69; 353.87] |
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 | 7.38810e-02 | |||
| Coefficient B | -3.01500e+02 | |||
| Coefficient C | 3.01190e-01 | |||
| Coefficient D | -6.84060e-03 | |||
| Coefficient E | -2.86460e-06 | |||
| Temperature range, min. | 279.69 | |||
| Temperature range, max. | 353.87 | |||
| λliquid | 0.13 | W/m×K | 279.69 | Calculated Property |
| λliquid | 0.13 | W/m×K | 287.93 | Calculated Property |
| λliquid | 0.12 | W/m×K | 296.17 | Calculated Property |
| λliquid | 0.12 | W/m×K | 304.42 | Calculated Property |
| λliquid | 0.12 | W/m×K | 312.66 | Calculated Property |
| λliquid | 0.12 | W/m×K | 320.90 | Calculated Property |
| λliquid | 0.12 | W/m×K | 329.14 | Calculated Property |
| λliquid | 0.11 | W/m×K | 337.39 | Calculated Property |
| λliquid | 0.11 | W/m×K | 345.63 | Calculated Property |
| λliquid | 0.11 | W/m×K | 353.87 | Calculated Property |
Similar Compounds
Find more compounds similar to Cyclohexane.
Mixtures
- Acetonitrile + Cyclohexane
- Benzene + Acetone + Cyclohexane
- Benzene + 2-Propanol + Acetone + Cyclohexane
- Acetone + Cyclohexane
- 2-Propanol + Acetone + Cyclohexane
- n-Hexane + Acetone + Cyclohexane
- n-Hexane + Acetone + Cyclohexane + Methyl Alcohol
- Acetone + Cyclohexane + Methyl Alcohol
- Benzene + Ethanol + Cyclohexane
- Ethanol + Cyclohexane
- Ethanol + Acetic acid, butyl ester + Cyclohexane + Water
- Ethanol + Tetrahydrofuran + Cyclohexane
- Ethanol + Cyclohexane + Water
- Benzene + Ethyl ether + Cyclohexane
- Ethyl ether + Cyclohexane
- Benzene + Ethyl Acetate + Cyclohexane
- Ethyl Acetate + Cyclohexane
- Ethyl Acetate + Tetrahydrofuran + Cyclohexane
- Benzene + 1-Butanol + Cyclohexane
- Benzene + Cyclohexane
Find more mixtures with Cyclohexane.
Sources
- KDB Vapor Pressure Data
- Active Thermochemical Tables 1.112, gas-phase enthalpies of formation ChEDL chemicals 1.5.2, from Active Thermochemical Tables (ATcT), version 1.112, Argonne National Laboratory; Ruscic, B. et al. Active Thermochemical Tables: Thermochemistry for the 21st Century. J. Phys.: Conf. Ser. 2005, 16, 561.
- 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.
- 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
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Densities, Viscosities, and Refractive Indices of Mixtures of Hexane with Cyclohexane, Decane, Hexadecane, and Squalane at 298.15K
- Speeds of Sound and Isentropic Compressibilities for Binary Mixtures of a Cyclic Diether with a Cyclic Compound at Three Temperatures
- Acoustic and Thermophysical Properties of Binary Liquid Mixtures of Primary Butanols with Hexane and Cyclohexane at 293.15 K
- Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
- Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
- Fluid Phase Topology of Benzene + Cyclohexane + 1-Propanol at 101.3 kPa
- Hydrogen solubility in a chemical hydrogen storage medium, aromatic hydrocarbon, cyclic hydrocarbon, and their mixture for fuel cell systems
- Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
- Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
- Activity coefficients in binary mixtures formed by cyclohexanone with a variety of compounds at 94.7 kPa
- Isobaric vapor liquid and vapor liquid liquid equilibrium data for the system water + ethanol + cyclohexane
- Vapour liquid equilibrium of carboxylic acid systems: Propionic acid + valeric acid and isobutyric acid + valeric acid
- Experimental and predicted vapour liquid equilibrium of 1,4-dioxane with cycloalkanes and benzene
- Experimental liquid liquid equilibria of 1-methylimidazole with hydrocarbons and ethers
- Deuterium isotope effects in liquid liquid phase diagrams of aniline + cyclohexane mixtures
- Experimental investigation of the vapour-liquid equilibrium of binary and ternary mixtures containing dibutyl ether (DBE), cyclohexane and toluene at 313.15 K
- Isobaric vapor liquid equilibria for ethanol water system containing different ionic liquids at atmospheric pressure
- Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
- Isobaric vapor liquid equilibria for binary systems of butyl chlorides with heptane, toluene and cyclohexane at 101.3, 80.0 and 53.3 kPa
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
- Experimental and predicted excess molar enthalpies for 1,4-dioxane + octane + cyclohexane at 303.15 K
- Excess enthalpies of binary mixtures of 2-ethoxyethanol with four hydrocarbons at 298.15, 308.15, and 318.15K An experimental and theoretical study
- Phase behaviour of I-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium based ionic liquids with alcohols, water, ketones and hydrocarbons: The effect of cation and anion on solubility
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
- Vapor liquid equilibrium for binary system of diethyl sulfide + cyclohexane at 353.15 and 343.15 K and diethyl sulfide + 2-ethoxy-2-methylpropane at 343.15 and 333.15 K
- Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
- Liquid liquid equilibrium of ternary systems containing nicotine
- Determination and correlation of liquid liquid equilibria for four binary N,N-dimethylformamide + hydrocarbon systems
- Solubility of naproxen in several organic solvents at different temperatures
- Hydrogen solubility of mixed naphthenes and aromatics for a new hydrogen storage medium in fuel cell system
- Liquid liquid equilibria of lactam containing binary systems
- Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
- Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
- Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
- Measurement and correlation of vapor pressure of benzene and thiophene with BMIM][PF6] and [BMIM][BF4] ionic liquids
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
- Isobaric vapor liquid equilibrium for binary mixtures of 1-hexene + n-hexane and cyclohexane + cyclohexene at 30, 60 and 101.3 kPa
- 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
- Liquid phase equilibria for mixtures of (an aliphatic hydrocarbon + toluene + gamma-butyrolactone)
- (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
- Experimental solid-liquid phase equilibria of {cholesterol + binary solvent mixture: 1-Alcohol (C4-C10) + cyclohexane}
- Thermodynamic analysis of the solubility of ketoprofen in some propylene glycol + water cosolvent mixtures
- Isobaric vapor-liquid equilibria for binary and ternary mixtures with cyclohexane, cyclohexene, and morpholine at 100 kPa
- Liquid-liquid equilibria for ternary systems of {cyclohexane + aromatic compounds + 1-ethyl-3-methylpyridinium ethylsulfate}
- Measurements of binary diffusion coefficients for metal complexes in organic solvents by the Taylor dispersion method
- Excess Gibbs energies and volumes of the ternary system chloroform + tetrahydrofuran + cyclohexane at 298.15 K
- "Vapor-liquid" equilibrium measurements and modeling for the cyclohexane + cyclohexanol binary system
- Solubility of benzoic acid in acetone, 2-propanol, acetic acid and cyclohexane: Experimental measurement and thermodynamic modeling
- 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
- Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
- 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
- Influence of anion structure on the liquid-liquid equilibria of 1-(3-hydroxypropyl)pyridinium cation based ionic liquid-hydrocarbon binary systems
- Solubility of decanedioic acid in binary solvent mixtures
- Vapor-liquid equilibrium measurements and modeling for the cyclohexane + n-hexanoic acid binary system
- Vapor liquid liquid equilibrium and vapor liquid equilibrium for the quaternary system water ethanol cyclohexane toluene and the ternary system water cyclohexane toluene. Isobaric experimental determination at 101.3 kPa
- Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
- Solubility of elemental sulfur in pure organic solvents and organic solvent-ionic liquid mixtures from 293.15 to 353.15 K
- Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
- 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
- Capacity of ionic liquids [EMim][NTf2] and [EMpy][NTf2] for extraction of toluene from mixtures with alkanes: Comparative study of the effect of the cation
- Thermodynamic characterization of second generation biofuels: Vapour-liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol and cyclohexane or toluene
- 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
- Effect of 1-methyl 3-octylimidazolium thiocyanate on vapor-liquid equilibria of binary mixtures of hydrocarbons
- Isobaric vapor-liquid-liquid equilibrium for water + cyclohexane + acetic acid at 101.3 kPa
- Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
- Enthalpies and Gibbs free energies of solvation in ethylene glycol at298 K: Influence of the solvophobic effect
- A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
- Phase equilibria and excess molar enthalpies study of the binary systems (pyrrole + hydrocarbon, or an alcohol) and modeling
- Experimental data, correlation and prediction of the extraction of benzene from cyclic hydrocarbons using [Epy][ESO4] ionic liquid
- Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
- Towards automated characterisation of liquid-liquid equilibria
- Volumetric investigation of the ternary system ethanol + dimethylformamide + cyclohexane at 298.15 K
- 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
- Isothermal vapour pressures and thermodynamic excess properties of 3,5- and 2,6-dimethylpyridine with cyclohexane. Measurements and prediction
- tert-Butyl chloride as a probe of the solvophobic effects
- Thermodynamic properties of cyclohexane methanol liquid mixture from shear viscosity measurements
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- The role of organic diluents in the aspects of equilibrium, kinetics and thermodynamic model for silver ion extraction using an extractant D2EHPA
- Distribution of cyclohexanol and cyclohexanone between water and cyclohexane
- Determination and correlation of solubility and solution thermodynamics of coumarin in different pure solvents
- Isothermal vapor- liquid equilibria and excess molar enthalpy of 2-methylpyrazine (2MP) containing binary mixtures. Comparison with DISQUAC predictions
- Mesoscale solubilization and critical phenomena in binary and quasi-binary solutions of hydrotropes
- Thermodynamics properties, VLE and HE, of the systems 2-pentanol and cyclohexane or methylbenzene for contributing to the knowledge of new biofuels
- Measurement and correlation of solid-liquid equilibria for three binaries, ethanol-antipyrine, chloroform-antipyrine, and dimethyl ether-antipyrine
- Solubilities of adipic acid in binary cyclohexanone + cyclohexanol, cyclohexane + cyclohexanol, and cyclohexane + cyclohexanone solvent mixtures
- 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
- Separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [EMIM]-based ionic liquids
- Measurement and prediction of liquid-liquid equilibria in ternary systems containing water, an organic component, and cyclohexanol
- In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
- Volume expansion prediction of supercritical CO 2 + crude oil
- 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
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Ternary LLE measurements for the separation of hex-1-ene/hexane and cyclohexene/cyclohexane compounds with [DCA]-based ionic liquids
- Plotting of phase (vapor-liquid) transition surface near the critical point out of data from isochoric experiment. Experimental procedure
- Quaternary isothermal vapor-liquid equilibrium of the model biofuel 2-butanone + n-heptane + tetrahydrofuran + cyclohexane using Raman spectroscopic characterization
- Measurement of critical properties for binary and ternary mixtures containing potential gasoline additive diethyl carbonate (DEC)
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Vapor-liquid equilibrium in the binary and ternary systems containing ethyl propionate, ethanol and alkane at 101.3 kPa
- 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
- Phase equilibria of 1-hexyl-3-methylimidazolium acetate with water and oil
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Study of molecular interactions and preferential solvation in binary mixtures of cyclohexane and (C5-C10) 1-alkanol by Kirkwood-Buff integrals
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
- The determination of activity coefficients at infinite dilution using g.l.c. for hydrocarbons in furfural at T = 278:15 K and T = 298:15 K
- Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
- Excess molar enthalpies of the ternary mixtures: (methyl tert-butyl ether or 2-methyltetrahydrofuran + cyclohexane + 2,2,4- trimethylpentane} at the temperature 298.15 K
- Dielectric study of molecular association in the binary mixtures (2-ethyl-1-hexanol + alcohol) and (cyclohexane + alcohol) at 298.2 K
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
- Liquid + liquid equilibria for ternary mixtures of (solvent + aromatic hydrocarbon + alkane)
- Excess molar volumes of the ternary system {methylcyclohexane (1) + cyclohexane (2) + n-alkanes (3)} at T = 298.15 K
- Partial molar volume of paracetamol in water, 0.1 M HCl and 0.154 M NaCl at T = (298.15, 303.15, 308.15 and 310.65) K and at 101.325 kPa
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
- 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)
- Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
- Thermophysical study of 1,4-dioxane with cycloalkane mixtures
- Azeotropic behaviour of (benzene + cyclohexane + chlorobenzene) ternary mixture using chlorobenzene as entrainer at 101.3 kPa
- Thermodynamic properties of binary mixtures of N-methyl-2-pyrrolidinone with cyclohexane, benzene, toluene at (303.15 to 353.15) K and atmospheric pressure
- Dynamic viscosities of binary mixtures of cycloalkanes with primary alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO interaction parameters
- Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- Mixing properties of binary mixtures presenting azeotropes at several temperatures
- Thermodynamic study of (perfluoroalkane + alkane) mixtures: Excess and solvation enthalpies
- (p,Vm,T) measurements of (cyclohexane + nonane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
- (Liquid + liquid) equilibria of [C8mim][NTf2] ionic liquid with a sulfur-component and hydrocarbons
- Densities, viscosities, and excess properties of (N-methylmorpholine + cyclohexane, + benzene, and + toluene) at T = (298.15, 303.15, 313.15, 323.15) K
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Measurement and correlation of (liquid + liquid) equilibrium of the azeotrope (cyclohexane + 2-butanone) with different ionic liquids at T = 298.15 K
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
- Evaluation of (vapor + liquid) equilibria for the binary systems (1-octanol + cyclohexane) and (1-octanol + n-hexane), at low alcohol compositions
- Thermodynamics of biofuels: Excess enthalpies for binary mixtures involving ethyl 1,1-dimethylethyl ether and hydrocarbons at different temperatures using a new flow calorimeter
- 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
- Thermodynamic properties of solvation of aromatic compounds in cyclohexane, heptane, benzene, 1,4-dioxane, and chloroform at 298.15 K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium trifluoromethanesulfonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- (Liquid + liquid) equilibria for ternary mixtures of (water + propionic acid + organic solvent) at T = 303.2 K
- (Liquid + liquid) equilibria of (heptane, or hexane, or cyclohexane + toluene + 1,3- dimethyl-2-imidazolidinone) ternary systems at T = 298.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- (Liquid + liquid) equilibria in ternary aqueous mixtures of phosphoric acid with organic solvents at T = 298.2 K
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Excess properties and vapour pressure of {3-diethylaminopropylamine + cyclohexane}
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- (Vapour + liquid) equilibria of ternary systems with ionic liquids using headspace gas chromatography
- A thermodynamic study on solubility and liquid-liquid phase behaviour for 2,2,2-trifluoroethanol + cyclohexane + 1-butanol at three temperatures and pressure 101.3 kPa
- 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
- Measurement and correlation of the (p, rho, T) relation of liquid cyclohexane, toluene, and ethanol in the temperature range from 233.15 K to 473.15 K at pressures up to 30 MPa for use as density reference liquids
- (Liquid + liquid) equilibria for mixtures of (ethylene glycol + benzene + cyclohexane) at temperatures (298.15, 308.15, and 318.15) K
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Relative permittivity data of binary mixtures containing 2-butanol, 2-butanone, and cyclohexane
- Thermodynamic properties of chiral fenchones in some solutions at T = 298.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
- 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
- Thermodynamic and topological investigations of molecular interactions in binary and ternary mixtures containing 1-methyl pyrrolidin-2-one at T = 308.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
- Measurement of (liquid + liquid) equilibria for ternary systems of (N-formylmorpholine + benzene + cyclohexane) at temperatures (303.15, 308.15, and 313.15) K
- Compressed liquid density measurements for {methylbenzoate + (cyclohexane or 1-hexanol)} binary systems
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Quaternary isobaric (vapor + liquid + liquid) equilibrium and (vapor + liquid) equilibrium for the system (water + ethanol + cyclohexane + heptane) at 101.3 kPa
- 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
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- 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
- (Liquid + liquid) equilibria for the ternary mixtures (alkane + toluene + ionic liquid) at T = 298.15 K: Influence of the anion on the phase equilibria
- Evaluation of the ionic liquids 1-alkyl-3-methylimidazolium hexafluorophosphate as a solvent for the extraction of benzene from cyclohexane: (Liquid + liquid) equilibria
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- (Liquid + liquid) equilibria of {benzene + cyclohexane + two ionic liquids} at different temperature and atmospheric pressure
- 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
- Experimental study on vapor-liquid equilibria of ternary systems of hydrocarbons/ionic liquid using headspace gas chromatography
- 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
- (Liquid + liquid) equilibrium data of (water + phosphoric acid + solvents) systems at T = (308.2 and 318.2) K
- Application of [HMim][NTf2], [HMim][TfO] and [BMim][TfO] ionic liquids on the extraction of toluene from alkanes: Effect of the anion and the alkyl chain length of the cation on the LLE
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Excess properties and vapour pressure of 2-diethylaminoethylamine + cyclohexane
- Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
- Heat capacities and densities of the binary mixtures containing ethanol, cyclohexane or 1-hexene at high pressures
- 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
- Volumetric and acoustic properties of binary mixtures of tri-n-butyl phosphate with n-hexane, cyclohexane, and n-heptane from T = (298.15 to 323.15) K
- 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
- Isothermal (vapour + liquid) equilibria for binary mixtures of diisopropyl ether with (methanol, or ethanol, or 1-butanol): Experimental data, correlations, and predictions
- Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- Measurement of critical temperatures and critical pressures for binary mixtures of methyl tert-butyl ether (MTBE) + alcohol and MTBE + alkane
- Phase equilibria study of the (N-octylisoquinolinium thiocyanate ionic liquid + aliphatic and aromatic hydrocarbon, or thiophene) binary systems
- Thermodynamics of solvation and solvophobic effect in formamide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
- 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
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide 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
- Contribution to study of the thermodynamics properties of mixtures containing 2-methoxy-2-methylpropane, alkanol, alkane
- Densities, viscosities, and isobaric heat capacities of the system (1-butanol + cyclohexane) at high pressures
- Quaternary (liquid + liquid) equilibrium data for the extraction of toluene from alkanes using the ionic liquid [EMim][MSO4]
- 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
- Excess enthalpy for the (benzene + cyclohexane) mixture over a wide range of temperature and pressure
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Excess molar volumes and excess isentropic compressibilities of binary and ternary mixtures of o-chlorotoluene with cyclic ether and amides or cyclohexane at different temperatures
- Pressure dependence of excess enthalpy for (benzene + cyclohexane) mixture near the critical locus at T = (558.2, 563.2 and 573.2) K and p = (3 to 15) MPa
- (Liquid + liquid) equilibria for (benzene + cyclohexane + dimethyl sulfoxide) system at T = (298.15 or 303.15) K: Experimental data and correlation
- 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
- Measurements and modeling of LLE and HE for (methanol + 2,4,4-trimethyl-1-pentene), and LLE for (water + methanol + 2,4,4-trimethyl-1-pentene)
- 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
- Volumetric, acoustic, and refractometric properties of (thiophene + hexane/cyclohexane) solutions in the presence of some imidazolium based ionic liquids at T = 298.15 K
- Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
- Study of the binary mixtures of {monoglyme + (hexane, cyclohexane, octane, dodecane)} by ECM-average and PFP models
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
- 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
- (Vapour + liquid) equilibria, (VLE) excess molar enthalpies and infinite dilution activity coefficients of selected binary systems involving n-hexyl pyridinium bis(trifluoromethylsulphonyl)imide ionic liquid: Experimental and predictions using modified UNIFAC (Dortmund)
- The effect of the naphthenic ring on the VLE of (carbon dioxide + alkane) mixtures
- Modified solution calorimetry approach for determination of vaporization and sublimation enthalpies of branched-chain aliphatic and alkyl aromatic compounds at T = 298.15 K
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- 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
- (Liquid + liquid) equilibrium of ternary and quaternary systems containing heptane, cyclohexane, toluene and the ionic liquid [EMim][N(CN)2]. Experimental data and correlation
- Selective recovery of aliphatics from aromatics in the presence of the {[4empy][Tf2N] + [emim][DCA]} ionic liquid mixture
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
- Measurement and correlation of solubility of pronamide in five organic solvents at (278.15-323.15) K
- Determination and correlation of solubility and thermodynamic properties of pyraclostrobin in pure and binary solvents
- Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
- Adamantanes: Benchmarking of thermochemical properties
- Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
- Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- 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
- Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
- Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
- Bis(trifluoromethylsulfonyl)imide, or dicyanamide-based ionic liquids in the liquid liquid extraction of hex-1-ene from hexane and cyclohexene from cyclohexane
- Liquid-liquid separation of hex-1-ene from hexane and cyclohexene from cyclohexane with ionic liquids
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
- Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Effect of temperature on intermolecular interactions between the organic solvents: Insights from density and excess volume
- Liquid-liquid separation of hexane/hex-1-ene and cyclohexane/cyclohexene by dicyanamide-based ionic liquids
- 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
- The contour of excess molar enthalpy at a mole fraction of benzene x = 0.548 on the p-T plane in liquid state and near the critical points for the (benzene + cyclohexane) mixture
- 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
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
- 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
- Imidazolium and pyridinium-based ionic liquids for the cyclohexane/cyclohexene separation by liquid-liquid extraction
- Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
- Isobaric vapor-liquid equilibrium of three binary systems containing dimethyl succinate, dimethyl glutarate and dimethyl adipate at 2, 5.2 and 8.3 kPa
- Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
- Densities, isobaric thermal compressibilities and derived thermodynamic properties of the binary systems of cyclohexane with allyl methacrylate, butyl methacrylate, methacrylic acid, and vinyl acetate at t = (298.15 and 308.15)K
- Volumetric and viscometric studies of molecular interaction of the ternary system toluene (1) + cyclohexane (2) + n-hexane (3) at 298.15K
- Studies of partial molar volumes of alkylamine in non-electrolyte solvents I. Alkylamines in hydrocarbons at 303.15 and 313.15K
- Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
- Liquid liquid equilibria for mixtures of (ethylene carbonate + aromatic hydrocarbon + cyclohexane)
- Thermophysical properties and thermodynamic phase behavior of ionic liquids
- Topological and thermodynamic investigations of binary mixtures: Molar excess volumes, molar excess enthalpies and isentropic compressibility changes of mixing
- Volumetric and transport properties of ternary mixtures containing 1-propanol, triethylamine or tri-n-butylamine and cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Excess molar volumes and isentropic compressibilities changes of mixing of tetrahydropyran + benzene + cyclo or n-alkanes ternary mixtures at 308.15 K
- Thermodynamic properties of binary mixtures containing Tetrahydropyran: Excess molar volumes, Excess molar enthalpies and isentropic compressibilities changes of mixing
- THERMODYNAMICS OF MIXTURES CONTAINING ALKOXYETHANOLS. XXVIII. LIQUID-LIQUID EQUILIBRIA FOR 2-PHENOXYETHANOL + SELECTED ALKANES
- Phase diagrams for the aqueous solutions of butyric acid with cyclohexane at different temperatures: Experimental and correlated data
- Thermodynamic functions of hydrogen bonding of amines in methanol: head space analysis and solution calorimetry
- Volumetric and Acoustic Properties of Binary Mixtures of Cyclohexane + Benzene and + Benzaldehyde at (293.15 to 323.15) K
- Temperature dependence of densities, speeds of sound, and derived properties of cyclohexylamine + cyclohexane or benzene in the range (293.15 to 323.15) K
- Development of a certified reference material for calibration of DSC and DTA below room temperature: NMIJ CRM 5401-a, Cyclohexane for Thermal Analysis
- Solvation of N-methyl-2-pyrrolidone and N,N-dimethylpropanamide in cyclohexane, heptane, n-alkan-1-ols(C1-C4) and water at 298.15K
- Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Use of quantitative structure property relationships to study the solvation process of 18-crown-6
- Standard molar Gibbs free energy and enthalpy of solvation of lowpolar solutes in formamide derivatives at 298 K
- Six-membered ring aliphatic compounds: A search for regularities in phase transitions
- Thermochemistry of hydrogen bonding of linear and cyclic amides inproton acceptors media
- A new analysis method for improving collection of vapor-liquid equilibrium (VLE) data of binary mixtures using differential scanning calorimetry (DSC)
- Solution and solvation enthalpies of aromatic derivitives in binary mixtures. Dipole moment and dielectric properties
- Vapor Liquid Equilibrium Data for Binary Systems of N,N-Dimethylacetamide with Cyclohexene, Cyclohexane, and Benzene Separately at Atmospheric Pressure
- Viscous Calibration Liquids for Self-diffusion Measurements
- Viscosities of liquid cyclohexane and decane at temperatures between (303 and 598) K and pressures up to 4 MPa measured in a dual-capillary viscometer
- Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
- Relative Permittivity and Apparent Dipole Moments of Nitromethane, Nitroethane, 1-Nitropropane and 2- Nitropropane in Several Nonpolar Solvents.
- Isobaric Vapor Liquid Liquid Equilibrium for Water + Cyclohexane + Acrylic Acid at 200 mmHg
- Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
- Liquid Liquid Equilibrium data for the ternary systems of Water, Isopropyl alcohol, and selected entrainers
- Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
- Experimental and Computational Study on Liquid Liquid Equilibrium in Ternary Systems of -Valerolactone, Toluene, and Hydrocarbons
- Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
- Solubilities of Adipic Acid in Cyclohexanol + Cyclohexanone Mixtures and Cyclohexanone + Cyclohexane Mixtures
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Vapor Liquid Equilibria for (n-Hexane, n-Octane, Cyclohexane, or 2,3-Dimethylpentane) + Toluene + {[4empy][Tf2N] (0.3) + [emim][DCA] (0.7)} Mixed Ionic Liquids
- Design of Equilibrium Cells for Phase Equilibria and PVT Measurements in Large Ranges of Temperatures and Pressures. I. Vapor Liquid Liquid Equilibria
- Determination and Correlation of Vapor Liquid Equilibria for the Phosphoric Acid + Water + Cyclohexane + Ethanol System
- Determination and Correlation for the Solubility of Glutaric Acid in Cyclohexane + Cyclohexanol + Cyclohexanone Solvent Mixtures
- 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
- Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
- Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
- Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Measurement and Prediction of Vapor Liquid(-Liquid) Equilibria in Ternary Systems Containing Water, an Organic Component, and Cyclohexanol
- Influence of Temperature on the Liquid Liquid Phase Equilibria of Ternary (Water + Alcohol + Entrainer) Systems
- The Critical Temperatures of a Number of (i) (Chloroalkane (C3 C4) + Hydrocarbon (C6 C7)) Binary Mixtures and (ii) (Aromatic Halocarbon (Chlorobenzene, Fluorobenzene, 1,2-Dichlorobenzene, or 1,3-Dichlorobenzene) + Alkane (C8)) Binary Mixtures
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Extraction of Low Concentration Aqueous Solution of Methylal: Liquid Liquid Equilibrium in Water + Methylal + (Cyclohexane and n-Heptane) Ternary Systems
- Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
- Solubility Measurement and Correlation of Fosfomycin Sodium in Six Organic Solvents and Different Binary Solvents at Temperatures between 283.15 and 323.15 K
- Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
- Measurement and Prediction of Vapor-Liquid Equilibria in Ternary Systems Containing an Organic Component, Cyclohexylamine, and Cyclohexanol
- Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
- Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
- Mutual Solubilities of Cyclohexane and Water in Aqueous Methyldiethanolamine /Cyclohexane Liquid-Liquid Equilibria
- Determination and Correlation for the Solubilities of Succinic Acid in Cyclohexanol + Cyclohexanone + Cyclohexane Solvent Mixtures
- 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
- Measurement and Correlation of the Solubility of Pyrimethanil in Seven Monosolvents and Two Different Binary Mixed Solvents
- Bubble Pressure Measurement and Prediction for n-Hexadecane and n-Eicosane + Cyclohexane, Methylcyclohexane, and Ethylcyclohexane Binary Mixtures from 303.15 to 393.15 K
- Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
- Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
- Permittivities, Refractive Indices, Densities, and Excess Properties for Binary Systems Containing 1-Alkanols and Cyclopentanone
- Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
- Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Solubility of Diflufenican in Pure and Binary Solvent Systems
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
- Liquid-Liquid-Solid Equilibria in the Ternary System Water-Phosphoric Acid-Cyclohexane at 25 and 35 deg.C: Stability Domain of Hemihydrate and Anhydrous Phosphoric Acid
- Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
- Comparative Dielectric Study and Molecular Interactions of Binary Mixtures of (Cyclohexanone + 1-Alkanols) and (Cyclopentanone or Cyclohexanone + Cyclohexanol or Cyclohexane) at T = 298.15 K
- Total Pressure Phase Equilibrium Measurements for the Binary Systems of n-Pentane + Cyclohexane and 1-Hexene + 2-Propanol
- A New Test System for Distillation Efficiency Experiments at Elevated Liquid Viscosities: Vapor-Liquid Equilibrium and Liquid Viscosity Data for Cyclopentanol + Cyclohexanol
- Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
- Experimental Mutual Solubility Data for Cyclohexane and Water in Aqueous Solutions of Diethanolamine
- Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
- Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
- Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
- Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
- Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
- o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
- Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
- Liquid-Liquid Equilibria for Benzene/Thiophene + Cyclohexane/Hexadecane + Deep Eutectic Solvents: Data and Correlation
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- 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
- Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
- Solubility Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
- Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
- Determination and Modeling of d-Histidine Solubility in Several Pure Solvents from 293.15 to 333.15 K
- Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
- Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
- Solubility Data for Roflumilast and Maraviroc in Various Solvents between T = (278.2-323.2) K
- Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Effect of Composition and Temperature upon Density, Viscosity, Surface Tension, and Refractive Index of 2,2,4-Trimethylpentane + Cyclohexane + Decane Ternary Liquid Systems
- Liquid-Liquid Equilibria for the Binary Systems of N-Formylmorpholine with Cycloalkanes
- Viscosities of Dimethyl Carbonate or Diethyl Carbonate with Alkanes at Four Temperatures. New UNIFAC-VISCO Parameters
- Surface Tension of Pure Liquids and Binary Liquid Mixtures
- Solubility of 1-Alkyl-3-methylimidazolium Hexafluorophosphate in Hydrocarbons
- Bubble Temperature Measurements on Binary Mixtures Formed by Cyclohexane at 94.7 kPa
- Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
- Excess Enthalpies of the Ternary Mixtures: Tetrahydrofuran + (Hexane or Cyclohexane) + Decane at 298.15K
- Excess Molar Enthalpies for the Binary Systems of Benzene or Cyclohexane with 1,1-Diethoxyethane at 323.15 K or with 2,2-Dimethoxybutane at 303.15 K and Infinite Dilution Activity Coefficients in 1,1-Diethoxyethane
- An apparatus for the on-line GC determination of hydrocarbon solubility in water: benzene and cyclohexane from 70 C to 150 C
- Determination of Isobaric Thermal Expansivity of Organic Compounds from 0.1 to 30 MPa at 30 C with an Isothermal Pressure Scanning Microcalorimeter
- Vapor-Liquid Equilibrium in a Ternary System Cyclohexane + Ethanol + Water
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
- Critical Point Measurements for Five n-Alkylcyclohexanes (C6 to C10) by the Pulse-Heating Method
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Bubble-Temperature Measurements on Some Binary Mixtures Formed by Tetrahydrofuran or Amyl Alcohol with Hydrocarbons, Chlorohydrocarbons, or Butanols at (94.6 or 95.8) kPa
- Vapor-Liquid Equilibria in Alcohol + Cyclohexane + Water Systems
- Solubility of -Carotene in Binary Solvents Formed by Some Hydrocarbons with Dibutyl Ether and 1,2-Dimethoxyethane
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Hexyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography at the Temperatures 298.15 K and 323.15 K
- Partition Coefficients of Organic Solutes between Supercritical Carbon Dioxide and Water: Experimental Measurements and Empirical Correlations
- 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
- Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
- Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons
- Determination and Study on the Solubility of Methane in Heptane + Cyclohexane and Heptane + Ethanol at High Pressures
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- Vapor-Liquid Equilibria of the Binary System 1-Pentanol + Anisole and the Quaternary System Benzene+Cyclohexane+1-Pentanol+Anisole at 101.32 kPa
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with tert-Butyl Methyl Ether and with tert-Amyl Methyl Ether
- Phase Equilibria for the Ternary Liquid Systems of (Water + Tetrahydrofurfuryl Alcohol + Cyclic Solvent) at 298.2 K
- Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
- Thermophysical Properties of Binary Mixtures of Cyclohexane + Nitrobenzene, Cyclohexanone + Nitrobenzene, and Cyclohexane + Cyclohexanone at (298.15, 303.15, and 308.15) K
- Vapor-Liquid Equilibria and Excess Enthalpies for Binary Systems of Dimethoxymethane with Hydrocarbons
- Measurement of Diffusion Coefficients in Thermodynamically Nonideal Systems
- Solubility of Propyl p-hydroxybenzoate in Supercritical Carbon Dioxide with and without Cosolvent
- Thermodynamic Properties of Binary Mixtures of p-Xylene with Cyclohexane, Heptane, Octane, and N-Methyl-2-pyrrolidone at Several Temperatures
- Determination of Activity Coefficients at Infinite Dilution of Polar and Nonpolar Solutes in the Ionic Liquid 1-Ethyl-3-methyl- imidazolium Bis(trifluoromethylsulfonyl) Imidate Using Gas-Liquid Chromatography at the Temperature 303.15 K or 318.15 K
- VLE and LLE Data for the System Cyclohexane + Cyclohexene + Water + Cyclohexanol
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
- Critical Properties of the Reacting Mixture in the Selective Oxidation of Cyclohexane by Oxygen in the Presence of Carbon Dioxide
- Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
- Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
- Viscosities and Excess Molar Volumes of the Ternary System Toluene (1) + Cyclohexane (2) + Pentane (3) at 298.15 K
- Apparatus for the Determination of Water Solubility in Hydrocarbon: Toluene and Alkylcyclohexanes (C6 to C8) from 30 C to 180 C
- Liquid-Liquid Equilibria for Cyclohexane + Ethylbenzene + Sulfolane at (303.15, 313.15, and 323.15) K
- Solubility of p-Nitrobenzoic Acid in Supercritical Carbon Dioxide with and without Cosolvents
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Solubilities of Phenylphosphinic Acid, Hydroxymethylphenylphosphinic Acid, p-Methoxyphenylphosphinic Acid, p-Methoxyphenylhydroxymethylphosphinic Acid, Triphenylphosphine, Tri(p-methoxyphenyl)phosphine, and Tri(p-methoxyphenyl)phosphine Oxide in Selected Solvents
- Liquid-Liquid Equilibria for the Binary Systems of Sulfolane with Cycloalkanes
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Determination and Study of the Solubility of Methane in Mixtures of Methanol plus Various Hydrocarbons at High Pressures
- Liquid-Liquid Coexistence Curves for Binary Systems: Methanol + Cyclohexane and + Several Isomers of Hexane
- Viscosities, Densities, and Speed of Sound of the Cycloalkanes with Secondary Alcohols at T = (293.15, 298.15, and 303.15) K: New UNIFAC-VISCO Interaction Parameters
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Azeotropic and Heats of Mixing Data for Several Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibria of Ternary and Six-Component Systems Including Cyclohexane, Benzene, Toluene, Ethylbenzene, Cumene, and Sulfolane at 303.15 K
- Isothermal Vapor-Liquid Equilibria and Excess Enthalpies of (Propyl Ethanoate + Heptane), (Propyl Ethanoate + Cyclohexane), and (Propyl Ethanoate + 1-Hexene)
- Solid-Liquid Equilibria for Binary Organic Systems Containing 1-Methoxy-2-propanol and 2-Butoxy Ethanol
- Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
- Thermodynamics of Mixing Tetrahydropyran with 1-Alkanols and Excess Enthalpies of Homomorphy-Related Systems
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
- Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- High-Pressure Density Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
- Vapor-Liquid Equilibrium for Binary Systems of Cyclohexane + Cyclohexanone and + Cyclohexanol at Temperatures from (414.0 to 433.7) K
- Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Cosolvent Selection for Benzene-Cyclohexane Separation in Extractive Distillation
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Densities, Excess Molar Volumes, Isothermal Compressibilities, and Isobaric Expansivities of Dimethyl Carbonate + Cyclohexane Systems at Temperatures from (293.15 to 313.15) K and Pressures from (0.1 to 40) MPa
- 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 Equilibrium Measurements and Modeling for Cyclohexane + Cyclohexanone
- Liquid Extraction of Benzene from Its Mixtures Using 1-Ethyl-3-methylimidazolium Ethylsulfate as a Solvent
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Excess Gibbs Energies of the Ternary System 2-Methoxyethanol + Tetrahydrofuran + Cyclohexane and Other Relevant Binaries at 298.15 K
- Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
- Solubility of Benzoic Acid in Pure Solvents and Binary Mixtures
- Liquid-Liquid Equilibrium of (Water + Pentane-2,4-dione + Ethyl Ethanoate) and (Water + Pentane-2,4-dione + Cyclohexane) at (298.15 and 313.15) K
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and Methyl Isobutyl Ketone at 100 kPa
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Influence of Anion Structure on the Liquid-Liquid Equilibria of 1-Ethyl-3-methyl-imidazolium Cation Based Ionic Liquid-Hydrocarbon Binary Systems
- Isothermal Vapor-Liquid Equilibrium for Methanol and 2,3-Dimethyl-1-butene at 343.06 K, 353.27 K, 363.19 K, and 372.90 K
- Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
- Gas Solubility in Binary Liquid Mixtures: Carbon Dioxide in Cyclohexane + Cyclohexanone
- 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
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Interfacial Tensions of Imidazolium-Based Ionic Liquids with N-Alkanes and Cyclohexane
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Isobaric Vapor Liquid Equilibrium for Binary Systems of Toluene + Acrylic Acid, Toluene + Acetic Acid, and Cyclohexane + Acrylic Acid at 20 kPa
- Phase Equilibria Involved in the Extractive Distillation of Cyclohexane + Cyclohexene Using Diethyl Carbonate as an Entrainer
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
- Computer Aided Solvent scanning for the Separation of 2-methoxynaphthene and 2-acetyl-6-methoxynaphthalene
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Vapor Liquid Equilibria of Binary Mixtures Containing 2-Butanol and Hydrocarbons at 313.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
- Determination and Prediction of Vapor Liquid Equilibria for a System Containing Water + Butyl Acetate + Cyclohexane + Ethanol
- 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
- Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solubilities of Adipic Acid in Acetic Acid + Water Mixtures and Acetic Acid + Cyclohexane Mixtures
- A Promising Ionic Liquid [BMIM][FeCl4] for the Extractive Separation of Aromatic and Aliphatic Hydrocarbons
- Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
- Thermodynamics of Mixtures Containing Amines. XII. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for N-Methylaniline + Hydrocarbon Systems
- 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
- Vapor Liquid Equilibrium for Ternary and Binary Mixtures of Tetrahydrofuran, Cyclohexane, and 1,2-Propanediol at 101.3 kPa
- Liquid Liquid, Vapor Liquid, and Vapor Liquid Liquid Equilibrium Data for the Water n-Butanol Cyclohexane System at Atmospheric Pressure: Experimental Determination and Correlation
- Excess Molar Volume along with Viscosity and Refractive Index for Binary Systems of Tricyclo[5.2.1.0(2.6)]decane with Five Cycloalkanes
- Liquid Liquid Equilibrium for Ternary System Water + Cyclohexane + Acetic Acid at (303.2 to 333.2) K
- Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
- Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
- Excess Heat Capacities of Binary and Ternary Mixtures Containing 1-Ethyl-3-methylimidazolium Tetrafluoroborate and Anilines
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, 1,4-Dioxane and Piperidine) or (Cyclohexane, Morpholine and Piperidine) at 308.15 K and Atmospheric Pressure
- Solubilities of Succinic Acid in Acetic Acid + Water Mixtures and Acetic Acid + Cyclohexane Mixtures
- Design of a Gamma Densitometer for Hydrocarbon Fuel at High Temperature and Supercritical Pressure
- Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Ethanol + Cyclohexane Mixtures at (283.35 to 333.75) K
- Liquid Liquid Equilibria at Three Temperatures (between 280.15 K and 333.15 K) of Binary, Ternary, and Quaternary Systems Involving Monoethylene Glycol, Water, Cyclohexane, para-Xylene, trans- and cis-Dimethylcyclohexane, and trans- and cis-Decahydronaphthalene
- Selective Separation of Aromatics from Paraffins and Cycloalkanes Using Morpholinium-Based Ionic Liquid
- Vapor Liquid Equilibrium Measurements and Thermodynamic Modeling of the System (Methane + Cyclohexane + Ethanol)
- Binary Liquid Liquid Equilibria of ?-Valerolactone with Some Hydrocarbons
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Measurement and Correlation of Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Alkane and Cycloalkane Solvents
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- Liquid-Liquid Equilibria for Systems Composed by 1-Methyl-3-octylimidazolium Tetrafluoroborate Ionic Liquid, Thiophene, and n-Hexane or Cyclohexane
- Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Isobaric Vapor-Liquid Equilibrium for the Binary Systems 1-Pentanol + Cyclohexane and 1-Pentanol + n-Hexane at Low Alcohol Compositions
- 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
- Henry s Law Constants for Fragrance and Organic Solvent Compounds in Aqueous Industrial Surfactants
- Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
- Thermodynamics of Fuels with a Biosynthetic Component. II. Vapor Liquid Equilibrium Data for Binary and Ternary Mixtures Containing Ethyl 1,1-Dimethylethyl Ether, 1-Hexene, and Cyclohexane at T = 313.15 K
- Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
- Solubility of Losartan Potassium in Different Binary Solvents from (293.15 to 343.15) 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
- Liquid-Liquid Equilibrium for 2,2,2-Trifluoroethanol + Ethanol + Cyclohexane from (288.15 to 308.15) K
- Phase Equilibrium Properties of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and Heptane or 1-Hexene at T ) 313.15 K
- Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Methyl-3-methylimidazolium Dimethylphosphate or + 1-Ethyl-3-methylimidazolium Diethylphosphate
- 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
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid, Trihexyltetradecylphosphonium Bis(trifluoromethylsulfonyl) Imide, Using Gas-Liquid Chromatography at T ) (303.15, 308.15, 313.15, and 318.15) K
- Phase Behavior of the Reactant and Products of Cyclohexane Oxidation in Compressed CO2
- Liquid-Liquid Equilibrium of (Cyclohexane + 2,2,2-Trifluoroethanol) and (Cyclohexane + Methanol) from (278.15 to 318.15) K
- Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
- Effect of Temperature on Phase Equilibrium of the Mixed-Solvent System of (2,2,2-Trifluoroethanol + Methanol + Cyclohexane)
- Densities and Viscosities of Binary Mixtures of Tri-n-butyl Phosphate + Cyclohexane, + n-Heptane at T ) (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Ternary Liquid-Liquid Equilibria Measurement for Benzene + Cyclohexane + N-Methylimidazole, or N-Ethylimidazole, or N-Methylimidazolium Dibutylphosphate at 298.2 K and Atmospheric Pressure
- Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
- Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
- Densities and Viscosities of Binary Mixtures of Tris(2-ethylhexyl) Phosphate + Cyclohexane or n-Hexane at T ) (293.15, 298.15, and 303.15) K and p ) 0.1 MPa
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
- Excess Enthalpies of Binary and Ternary Mixtures Containing Dibutyl Ether, Cyclohexane, and 1-Butanol at 298.15 K
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
- Liquid Viscosities of Cyclohexane, Cyclohexane + Tetradecane, and Cyclohexane + Benzene from (313 to 393) K and Pressures Up to 60 MPa
- Volumetric Behavior of the Binary Mixtures of Methyl Ethyl Ketone with n-Hexane, Cyclohexane, and Benzene at T ) (303.15, 313.15, and 323.15) K
- Liquid Viscosities of the Ternary System Benzene + Cyclohexane + n-Tetradecane from (313 to 393) K and Pressures up to 60 MPa
- Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
- Density and Viscosity of Decalin, Cyclohexane, and Toluene Binary Mixtures at (283.15, 293.15, 303.15, 313.15, and 323.15) K
- High-Pressure Viscosity Measurements for the Binary System Cyclohexane + n-Hexadecane in the Temperature Range of (318.15 to 413.15) K
- Vapor-Liquid Equilibria in Binary Systems Formed by Cyclohexane with Alcohols
- Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and 1,4-Dioxane at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations
- Isobaric Vapor-Liquid Equilibria for Binary and Ternary Mixtures with Cyclohexane, Cyclohexene, and 2-Methoxyethanol at 100 kPa
- 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
- Liquid-Liquid Equilibria for Benzene + Cyclohexane + 1-Butyl-3-methylimidazolium Hexafluorophosphate
- Excess Molar Enthalpies for the Binary and Ternary Mixtures of Cyclohexane, Tetrahydropyran, and Piperidine at 308.15 K and Atmospheric Pressure: Experimental Measurements and Correlations
- Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
- Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
- Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
- (Liquid + Liquid) Equilibria of (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanone) and (Cyclohexane + Dimethyl Sulfoxide + Cyclohexanol) at T = 303.2 K
- Phase Equilibria for Liquid Mixtures of (an Alkane + Toluene + Dimethyl Phthalate)
- Isobaric Vapor-Liquid-Liquid Equilibrium and Vapor-Liquid Equilibrium for the Quaternary System Water-Ethanol-Cyclohexane-Isooctane at 101.3 kPa
- Density, Viscosity, and Speed of Sound of (Methyl Benzoate + Cyclohexane), (Methyl Benzoate + n-Hexane), (Methyl Benzoate + Heptane), and (Methyl Benzoate + Octane) at Temperatures of (303.15, 308.15, and 313.15) K
- Isobaric Vapor-Liquid Equilibria for (Acetic Acid + Cyclohexane) and (Cyclohexane + Acetylacetone) at a Pressure of 101.3 kPa and for (Acetic Acid + Acetylacetone) at a Pressure of 60.0 kPa
- 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
- Experimental Measurements and Correlations of Excess Molar Enthalpies for the Binary and Ternary Mixtures of (Cyclohexane, Tetrahydropyran, and Morpholine) or (Cyclohexane, 1,4-Dioxane, and Morpholine) at 308.15 K and Atmospheric Pressure
- 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
- Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) 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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