- InChI
- InChI=1S/C8H18/c1-7(2)6-8(3,4)5/h7H,6H2,1-5H3
- InChI Key
- NHTMVDHEPJAVLT-UHFFFAOYSA-N
- Formula
- C8H18
- SMILES
- CC(C)CC(C)(C)C
- Molecular Weight1
- 114.23
- CAS
- 540-84-1
- Other Names
-
- (CH3)2CHCH2C(CH3)3
- 2,2,4-Trimethylpentane
- ISOBUTYLTRIMETHYLMETHANE
- ISOOCTANE
- Isobutyltrimethylethane
- UN 1262
- ω : Acentric Factor.
- AP : Aniline Point (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- ν : Kinematic viscosity (m2/s).
- 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.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3030 | KDB | |
| AP | 352.650 | K | KDB |
| ΔcH°liquid | -5461.30 ± 1.30 | kJ/mol | NIST |
| ΔfG° | 13.69 | kJ/mol | KDB |
| Rg | 4.1710 | KDB | |
| Δc,grossH | 5461.33 | kJ/mol | KDB |
| Δc,netH | 5065.192 | kJ/mol | KDB |
| ΔfH°gas | [-224.30; -224.10] | kJ/mol |
|
| ΔfH°gas | -224.30 | kJ/mol | KDB |
| ΔfH°gas | -224.10 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -259.30 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 5.54 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [34.90; 35.24] | kJ/mol |
|
| ΔvapH° | 35.24 | kJ/mol | NIST |
| ΔvapH° | Outlier 34.90 | kJ/mol | NIST |
| ΔvapH° | 35.20 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.10 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.12 | kJ/mol | NIST |
| IE | [9.86; 9.91] | eV |
|
| IE | 9.89 ± 0.03 | eV | NIST |
| IE | 9.91 | eV | NIST |
| IE | 9.86 | eV | NIST |
| log10WS | [-4.74; -4.74] |
|
|
| log10WS | -4.74 | Aq. Sol... | |
| log10WS | -4.74 | Estimat... | |
| logPoct/wat | 3.079 | Crippen Calculated Property | |
| McVol | 123.580 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | [2564.33; 2583.79] | kPa |
|
| Pc | 2570.00 | kPa | KDB |
| Pc | 2570.00 | kPa | Critica... |
| Pc | 2570.00 ± 20.00 | kPa | NIST |
| Pc | 2567.60 ± 40.53 | kPa | NIST |
| Pc | 2564.33 ± 10.13 | kPa | NIST |
| Pc | Outlier 2583.79 ± 15.19 | kPa | NIST |
| ρc | [243.31; 244.45] | kg/m3 |
|
| ρc | 244.45 ± 2.28 | kg/m3 | NIST |
| ρc | 243.31 ± 4.57 | kg/m3 | NIST |
| ρc | 243.31 ± 3.43 | kg/m3 | NIST |
| Inp | [680.00; 703.10] |
|
|
| Inp | 692.70 | NIST | |
| Inp | 689.10 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 691.10 | NIST | |
| Inp | 689.90 | NIST | |
| Inp | 690.20 | NIST | |
| Inp | 690.60 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | 694.90 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 693.50 | NIST | |
| Inp | Outlier 697.70 | NIST | |
| Inp | Outlier 703.10 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 694.10 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 689.90 | NIST | |
| Inp | 692.20 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 686.60 | NIST | |
| Inp | 687.50 | NIST | |
| Inp | 688.60 | NIST | |
| Inp | 689.60 | NIST | |
| Inp | 690.70 | NIST | |
| Inp | 691.90 | NIST | |
| Inp | 691.40 | NIST | |
| Inp | 691.30 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 688.60 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 690.30 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | Outlier 699.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 696.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | Outlier 680.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 688.44 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 687.50 | NIST | |
| Inp | 683.91 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 684.80 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 684.38 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 692.70 | NIST | |
| Inp | 690.20 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 694.10 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 689.60 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 688.44 | NIST | |
| Inp | 684.80 | NIST | |
| I | [676.00; 711.00] |
|
|
| I | 676.00 | NIST | |
| I | 698.00 | NIST | |
| I | 711.00 | NIST | |
| I | 705.00 | NIST | |
| I | 711.00 | NIST | |
| S°liquid | [314.60; 328.03] | J/mol×K |
|
| S°liquid | 328.03 | J/mol×K | NIST |
| S°liquid | 314.60 | J/mol×K | NIST |
| Tboil | [371.45; 389.00] | K |
|
| Tboil | 372.37 | K | KDB |
| Tboil | 372.33 | K | Vapor l... |
| Tboil | 372.33 | K | Measure... |
| Tboil | 372.26 | K | Low-Pre... |
| Tboil | 372.35 | K | Vapor-L... |
| Tboil | 372.40 ± 0.20 | K | NIST |
| Tboil | 372.40 ± 0.20 | K | NIST |
| Tboil | 372.40 | K | NIST |
| Tboil | 372.40 | K | NIST |
| Tboil | 372.00 ± 0.15 | K | NIST |
| Tboil | 372.40 ± 0.15 | K | NIST |
| Tboil | 372.50 ± 0.25 | K | NIST |
| Tboil | 372.30 ± 0.30 | K | NIST |
| Tboil | 372.15 ± 0.50 | K | NIST |
| Tboil | 372.30 ± 0.50 | K | NIST |
| Tboil | 372.35 ± 0.30 | K | NIST |
| Tboil | 372.39 ± 0.20 | K | NIST |
| Tboil | 371.45 ± 0.60 | K | NIST |
| Tboil | 372.15 ± 0.40 | K | NIST |
| Tboil | 372.30 ± 0.20 | K | NIST |
| Tboil | 372.40 ± 0.60 | K | NIST |
| Tboil | 372.37 ± 0.20 | K | NIST |
| Tboil | 372.38 ± 0.05 | K | NIST |
| Tboil | 372.39 ± 0.10 | K | NIST |
| Tboil | 372.65 ± 2.00 | K | NIST |
| Tboil | 372.15 ± 2.00 | K | NIST |
| Tboil | 372.35 ± 0.40 | K | NIST |
| Tboil | 372.45 ± 0.30 | K | NIST |
| Tboil | 372.50 ± 0.40 | K | NIST |
| Tboil | 372.38 ± 0.27 | K | NIST |
| Tboil | 372.38 ± 0.20 | K | NIST |
| Tboil | 372.38 ± 0.15 | K | NIST |
| Tboil | 372.45 ± 0.50 | K | NIST |
| Tboil | 372.38 ± 0.10 | K | NIST |
| Tboil | 372.38 ± 0.01 | K | NIST |
| Tboil | 372.39 ± 0.25 | K | NIST |
| Tboil | 372.38 ± 0.10 | K | NIST |
| Tboil | 372.45 ± 0.50 | K | NIST |
| Tboil | 372.39 ± 0.07 | K | NIST |
| Tboil | 372.50 ± 0.20 | K | NIST |
| Tboil | 372.55 ± 0.20 | K | NIST |
| Tboil | 372.39 ± 0.05 | K | NIST |
| Tboil | 372.38 ± 0.05 | K | NIST |
| Tboil | 372.39 ± 0.20 | K | NIST |
| Tboil | 372.55 ± 0.30 | K | NIST |
| Tboil | 372.38 ± 0.03 | K | NIST |
| Tboil | 372.25 ± 0.50 | K | NIST |
| Tboil | 372.25 ± 0.20 | K | NIST |
| Tboil | 372.38 ± 0.10 | K | NIST |
| Tboil | 372.38 ± 0.10 | K | NIST |
| Tboil | 372.40 ± 0.40 | K | NIST |
| Tboil | 372.25 ± 0.20 | K | NIST |
| Tboil | 372.65 ± 2.00 | K | NIST |
| Tboil | 372.35 ± 0.50 | K | NIST |
| Tboil | 372.45 ± 0.40 | K | NIST |
| Tboil | 372.45 ± 0.50 | K | NIST |
| Tboil | Outlier 389.00 ± 2.00 | K | NIST |
| Tc | [543.61; 544.30] | K |
|
| Tc | 543.80 | K | KDB |
| Tc | 544.00 | K | The Cri... |
| Tc | 543.80 ± 0.30 | K | NIST |
| Tc | 543.90 | K | NIST |
| Tc | 543.89 ± 0.40 | K | NIST |
| Tc | 543.61 ± 0.20 | K | NIST |
| Tc | 543.82 ± 0.10 | K | NIST |
| Tc | Outlier 544.30 ± 0.20 | K | NIST |
| Tfus | [165.00; 166.15] | K |
|
| Tfus | 165.80 | K | KDB |
| Tfus | Outlier 166.07 | K | Aq. Sol... |
| Tfus | 165.78 ± 0.10 | K | NIST |
| Tfus | 165.75 ± 0.04 | K | NIST |
| Tfus | 165.76 ± 0.02 | K | NIST |
| Tfus | 165.75 ± 0.02 | K | NIST |
| Tfus | 165.76 ± 0.02 | K | NIST |
| Tfus | 165.73 ± 0.10 | K | NIST |
| Tfus | 165.73 ± 0.10 | K | NIST |
| Tfus | 165.73 ± 0.10 | K | NIST |
| Tfus | 165.73 ± 0.06 | K | NIST |
| Tfus | 165.73 ± 0.06 | K | NIST |
| Tfus | 165.73 ± 0.06 | K | NIST |
| Tfus | 165.77 ± 0.09 | K | NIST |
| Tfus | 165.77 ± 0.05 | K | NIST |
| Tfus | 165.76 ± 0.06 | K | NIST |
| Tfus | 165.76 ± 0.03 | K | NIST |
| Tfus | 165.85 ± 0.20 | K | NIST |
| Tfus | 165.73 ± 0.10 | K | NIST |
| Tfus | 165.76 ± 0.06 | K | NIST |
| Tfus | 165.75 ± 0.15 | K | NIST |
| Tfus | 165.76 ± 0.03 | K | NIST |
| Tfus | 165.77 ± 0.02 | K | NIST |
| Tfus | 165.73 ± 0.15 | K | NIST |
| Tfus | 165.75 ± 0.30 | K | NIST |
| Tfus | 165.75 ± 0.12 | K | NIST |
| Tfus | 165.77 ± 0.05 | K | NIST |
| Tfus | 165.78 ± 0.03 | K | NIST |
| Tfus | 165.75 ± 0.04 | K | NIST |
| Tfus | 165.77 ± 0.02 | K | NIST |
| Tfus | 165.78 ± 0.20 | K | NIST |
| Tfus | 165.75 ± 0.01 | K | NIST |
| Tfus | 165.83 ± 0.30 | K | NIST |
| Tfus | 165.83 ± 0.30 | K | NIST |
| Tfus | 165.75 ± 0.50 | K | NIST |
| Tfus | 165.78 ± 0.20 | K | NIST |
| Tfus | 165.78 ± 0.07 | K | NIST |
| Tfus | 165.55 ± 0.40 | K | NIST |
| Tfus | 165.83 ± 0.20 | K | NIST |
| Tfus | 165.55 ± 0.20 | K | NIST |
| Tfus | 165.84 ± 0.06 | K | NIST |
| Tfus | Outlier 166.15 ± 2.00 | K | NIST |
| Tfus | Outlier 165.00 ± 2.00 | K | NIST |
| Tfus | 165.65 ± 0.50 | K | NIST |
| Tfus | 165.45 ± 0.40 | K | NIST |
| Tfus | Outlier 165.35 ± 0.50 | K | NIST |
| Ttriple | [165.30; 165.76] | K |
|
| Ttriple | 165.76 ± 0.40 | K | NIST |
| Ttriple | 165.30 ± 0.20 | K | NIST |
| Vc | [0.468; 0.482] | m3/kmol |
|
| Vc | 0.468 | m3/kmol | KDB |
| Vc | 0.468 | m3/kmol | NIST |
| Vc | 0.482 ± 0.020 | m3/kmol | NIST |
| Zc | 0.2660130 | KDB | |
| Zra | 0.27 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [233.00; 313.27] | J/mol×K | [378.77; 557.09] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 240 260 280 300 320 400 450 500 550 | ||||
| Cp,gas | 233.00 | J/mol×K | 378.77 | Joback Calculated Property |
| Cp,gas | 248.05 | J/mol×K | 408.49 | Joback Calculated Property |
| Cp,gas | 262.39 | J/mol×K | 438.21 | Joback Calculated Property |
| Cp,gas | 276.06 | J/mol×K | 467.93 | Joback Calculated Property |
| Cp,gas | 289.08 | J/mol×K | 497.65 | Joback Calculated Property |
| Cp,gas | 301.48 | J/mol×K | 527.37 | Joback Calculated Property |
| Cp,gas | 313.27 | J/mol×K | 557.09 | Joback Calculated Property |
| Cp,liquid | [233.70; 242.49] | J/mol×K | [293.15; 301.90] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 234 236 238 240 242 295 300 | ||||
| Cp,liquid | 237.85 | J/mol×K | 293.15 | NIST |
| Cp,liquid | 233.90 | J/mol×K | 295.20 | NIST |
| Cp,liquid | 242.49 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 242.49 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 239.71 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 237.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 237.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 238.57 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 238.87 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 233.70 | J/mol×K | 300.00 | NIST |
| Cp,liquid | 241.00 | J/mol×K | 301.90 | NIST |
| η | [0.0003690; 0.0005439] | Pa×s | [288.15; 323.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 4.00e-4 4.50e-4 5.00e-4 5.50e-4 290 300 310 320 | ||||
| η | 0.0005439 | Pa×s | 288.15 | Densiti... |
| η | 0.0005125 | Pa×s | 293.15 | Densiti... |
| η | 0.0004844 | Pa×s | 298.15 | Densiti... |
| η | 0.0004780 | Pa×s | 298.15 | Densiti... |
| η | 0.0004586 | Pa×s | 303.15 | Densiti... |
| η | 0.0004530 | Pa×s | 303.15 | Densiti... |
| η | 0.0004216 | Pa×s | 308.15 | Densiti... |
| η | 0.0004290 | Pa×s | 308.15 | Densiti... |
| η | 0.0004130 | Pa×s | 313.15 | Densiti... |
| η | 0.0004080 | Pa×s | 313.15 | Densiti... |
| η | 0.0003880 | Pa×s | 318.15 | Densiti... |
| η | 0.0003690 | Pa×s | 323.15 | Densiti... |
| ΔfusH | [9.04; 9.21] | kJ/mol | [165.30; 165.80] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 9.05 9.1 9.15 9.2 165.4 165.60000000000002 165.8 | ||||
| ΔfusH | 9.04 | kJ/mol | 165.30 | NIST |
| ΔfusH | 9.04 | kJ/mol | 165.30 | NIST |
| ΔfusH | 9.04 | kJ/mol | 165.30 | NIST |
| ΔfusH | 9.21 | kJ/mol | 165.79 | NIST |
| ΔfusH | 9.20 | kJ/mol | 165.80 | NIST |
| ΔvapH | [30.79; 40.70] | kJ/mol | [246.50; 517.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 32 34 36 38 40 300 400 500 | ||||
| ΔvapH | 40.70 | kJ/mol | 246.50 | NIST |
| ΔvapH | 36.10 | kJ/mol | 311.00 | NIST |
| ΔvapH | 34.40 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 34.30 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 33.40 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 33.20 ± 0.10 | kJ/mol | 333.00 | NIST |
| ΔvapH | 34.80 | kJ/mol | 335.50 | NIST |
| ΔvapH | 32.60 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 32.00 ± 0.10 | kJ/mol | 353.00 | NIST |
| ΔvapH | 31.70 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 33.90 | kJ/mol | 358.50 | NIST |
| ΔvapH | 31.00 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 31.00 | kJ/mol | 371.00 | NIST |
| ΔvapH | 31.01 | kJ/mol | 372.40 | KDB |
| ΔvapH | 30.79 | kJ/mol | 372.40 | NIST |
| ΔvapH | 32.20 | kJ/mol | 394.00 | NIST |
| ΔvapH | 31.50 | kJ/mol | 453.50 | NIST |
| ΔvapH | 31.60 | kJ/mol | 473.00 | NIST |
| ΔvapH | 31.40 | kJ/mol | 517.00 | NIST |
| ν | [0.0000005; 0.0000007] | m2/s | [293.15; 323.15] |
|
|
T(K) Kinematic viscosity (m2/s) 5.50e-7 6.00e-7 6.50e-7 7.00e-7 7.50e-7 300 310 320 | ||||
| ν | 0.0000007 | m2/s | 293.15 | Density... |
| ν | 0.0000007 | m2/s | 298.15 | Density... |
| ν | 0.0000007 | m2/s | 303.15 | Density... |
| ν | 0.0000006 | m2/s | 313.15 | Density... |
| ν | 0.0000005 | m2/s | 323.15 | Density... |
| Pvap | [3.05; 282.80] | kPa | [283.60; 413.15] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 300 350 400 | ||||
| Pvap | 3.05 | kPa | 283.60 | A milli... |
| Pvap | 3.99 | kPa | 288.40 | A milli... |
| Pvap | 5.18 | kPa | 293.40 | A milli... |
| Pvap | 6.63 | kPa | 298.30 | A milli... |
| Pvap | 6.62 | kPa | 298.40 | A milli... |
| Pvap | 8.33 | kPa | 303.15 | Measure... |
| Pvap | 8.39 | kPa | 303.30 | A milli... |
| Pvap | 10.44 | kPa | 308.15 | Measure... |
| Pvap | 10.53 | kPa | 308.20 | A milli... |
| Pvap | 12.97 | kPa | 313.10 | A milli... |
| Pvap | 12.97 | kPa | 313.15 | Measure... |
| Pvap | 12.97 | kPa | 313.15 | Thermod... |
| Pvap | 12.95 | kPa | 313.15 | Phase e... |
| Pvap | 12.96 | kPa | 313.15 | Vapor L... |
| Pvap | 13.01 | kPa | 313.15 | Vapor-L... |
| Pvap | 12.95 | kPa | 313.15 | Vapour-... |
| Pvap | 15.96 | kPa | 318.10 | A milli... |
| Pvap | 15.98 | kPa | 318.15 | Measure... |
| Pvap | 19.54 | kPa | 323.00 | A milli... |
| Pvap | 19.54 | kPa | 323.15 | Measure... |
| Pvap | 20.00 | kPa | 323.65 | Measure... |
| Pvap | 23.81 | kPa | 328.00 | A milli... |
| Pvap | 28.66 | kPa | 332.80 | A milli... |
| Pvap | 100.05 | kPa | 371.55 | Isobari... |
| Pvap | 101.30 | kPa | 372.26 | Low-Pre... |
| Pvap | 101.30 | kPa | 372.33 | Measure... |
| Pvap | 101.33 | kPa | 372.35 | Vapor-L... |
| Pvap | 103.49 | kPa | 373.10 | Phase E... |
| Pvap | 104.94 | kPa | 373.40 | Isobari... |
| Pvap | 124.90 | kPa | 379.80 | Isobari... |
| Pvap | 149.96 | kPa | 386.94 | Isobari... |
| Pvap | 174.70 | kPa | 393.14 | Isobari... |
| Pvap | 199.94 | kPa | 398.64 | Isobari... |
| Pvap | 224.91 | kPa | 403.68 | Isobari... |
| Pvap | 249.95 | kPa | 408.28 | Isobari... |
| Pvap | 250.00 | kPa | 408.30 | Isobari... |
| Pvap | 282.80 | kPa | 413.15 | Phase E... |
| n0 | [1.37898; 1.39404] | [288.15; 318.15] |
|
|
|
T(K) Refractive Index 1.38 1.39 1.39 1.4 290 300 310 | ||||
| n0 | 1.39404 | 288.15 | Densiti... | |
| n0 | 1.39404 | 288.15 | Densiti... | |
| n0 | 1.38894 | 293.15 | Isother... | |
| n0 | 1.38921 | 298.10 | Liquid-... | |
| n0 | 1.38905 | 298.15 | Volumet... | |
| n0 | 1.38917 | 298.15 | Liquid ... | |
| n0 | 1.38898 | 298.15 | Isother... | |
| n0 | 1.38890 | 298.15 | Phase e... | |
| n0 | 1.38890 | 298.15 | Excess ... | |
| n0 | 1.38800 | 298.15 | Excess ... | |
| n0 | 1.38887 | 298.15 | Vapor-L... | |
| n0 | 1.38894 | 298.15 | Isother... | |
| n0 | 1.38890 | 298.15 | (Vapor ... | |
| n0 | 1.38900 | 298.15 | Vapor l... | |
| n0 | 1.38894 | 298.15 | Isother... | |
| n0 | 1.38904 | 298.15 | (Vapour... | |
| n0 | 1.38901 | 298.15 | Volumet... | |
| n0 | 1.38887 | 298.15 | Vapor l... | |
| n0 | 1.38920 | 298.15 | Isother... | |
| n0 | 1.38905 | 298.15 | Measure... | |
| n0 | 1.38902 | 298.15 | Densiti... | |
| n0 | 1.38887 | 298.15 | Isobari... | |
| n0 | 1.38900 | 298.15 | Densiti... | |
| n0 | 1.38900 | 298.15 | Vapor-L... | |
| n0 | 1.38898 | 298.15 | Densiti... | |
| n0 | 1.38900 | 298.15 | Densiti... | |
| n0 | 1.38900 | 298.15 | A Study... | |
| n0 | 1.38898 | 298.15 | KDB | |
| n0 | 1.38910 | 298.20 | Vapor-L... | |
| n0 | 1.38520 | 303.15 | Excess ... | |
| n0 | 1.38395 | 308.15 | Densiti... | |
| n0 | 1.38395 | 308.15 | Densiti... | |
| n0 | 1.38240 | 308.15 | Excess ... | |
| n0 | 1.38398 | 308.15 | Densiti... | |
| n0 | 1.37898 | 318.15 | Densiti... | |
| ρl | [649.40; 704.10] | kg/m3 | [278.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 650 660 670 680 690 700 280 300 320 340 | ||||
| ρl | 704.10 | kg/m3 | 278.15 | Advance... |
| ρl | 700.05 | kg/m3 | 283.15 | Advance... |
| ρl | 695.98 | kg/m3 | 288.15 | Advance... |
| ρl | 691.88 | kg/m3 | 293.00 | Volumet... |
| ρl | 692.00 | kg/m3 | 293.00 | KDB |
| ρl | 691.83 | kg/m3 | 293.15 | Density... |
| ρl | 692.05 | kg/m3 | 293.15 | Isother... |
| ρl | 691.89 | kg/m3 | 293.15 | Advance... |
| ρl | 691.91 | kg/m3 | 293.15 | Densiti... |
| ρl | 692.00 | kg/m3 | 293.15 | Experim... |
| ρl | 691.84 | kg/m3 | 293.15 | Density... |
| ρl | 690.40 | kg/m3 | 295.00 | High-pr... |
| ρl | 687.77 | kg/m3 | 298.15 | Thermod... |
| ρl | 687.62 | kg/m3 | 298.15 | Excess ... |
| ρl | 687.32 | kg/m3 | 298.15 | Liquid-... |
| ρl | 687.76 | kg/m3 | 298.15 | Thermod... |
| ρl | 687.81 | kg/m3 | 298.15 | Liquid ... |
| ρl | 687.82 | kg/m3 | 298.15 | Densiti... |
| ρl | 688.03 | kg/m3 | 298.15 | Excess ... |
| ρl | 687.77 | kg/m3 | 298.15 | Advance... |
| ρl | 687.82 | kg/m3 | 298.15 | Isobari... |
| ρl | 688.18 | kg/m3 | 298.15 | Binary ... |
| ρl | 687.91 | kg/m3 | 298.15 | Liquid ... |
| ρl | 687.72 | kg/m3 | 298.15 | Phase e... |
| ρl | 687.74 | kg/m3 | 298.15 | Density... |
| ρl | 687.32 | kg/m3 | 298.15 | Thermod... |
| ρl | 687.70 | kg/m3 | 298.15 | Density... |
| ρl | 687.72 | kg/m3 | 298.20 | Apparen... |
| ρl | 683.64 | kg/m3 | 303.00 | Volumet... |
| ρl | 683.74 | kg/m3 | 303.15 | Isother... |
| ρl | 683.59 | kg/m3 | 303.15 | Density... |
| ρl | 683.64 | kg/m3 | 303.15 | Advance... |
| ρl | 683.68 | kg/m3 | 303.15 | Densiti... |
| ρl | 683.61 | kg/m3 | 303.15 | Density... |
| ρl | 679.48 | kg/m3 | 308.15 | Advance... |
| ρl | 679.40 | kg/m3 | 308.15 | Density... |
| ρl | 679.47 | kg/m3 | 308.15 | Density... |
| ρl | 679.51 | kg/m3 | 308.15 | Densiti... |
| ρl | 675.30 | kg/m3 | 313.00 | Volumet... |
| ρl | 675.29 | kg/m3 | 313.15 | Density... |
| ρl | 675.23 | kg/m3 | 313.15 | Density... |
| ρl | 675.28 | kg/m3 | 313.15 | Advance... |
| ρl | 675.32 | kg/m3 | 313.15 | Densiti... |
| ρl | 675.23 | kg/m3 | 313.20 | Apparen... |
| ρl | 670.98 | kg/m3 | 318.15 | Density... |
| ρl | 671.05 | kg/m3 | 318.15 | Densiti... |
| ρl | 671.09 | kg/m3 | 318.15 | Density... |
| ρl | 671.07 | kg/m3 | 318.15 | Advance... |
| ρl | 666.84 | kg/m3 | 323.00 | Volumet... |
| ρl | 666.80 | kg/m3 | 323.15 | Densiti... |
| ρl | 666.81 | kg/m3 | 323.15 | Advance... |
| ρl | 666.75 | kg/m3 | 323.15 | Density... |
| ρl | 666.86 | kg/m3 | 323.15 | Density... |
| ρl | 662.44 | kg/m3 | 328.15 | Density... |
| ρl | 662.52 | kg/m3 | 328.15 | Advance... |
| ρl | 658.20 | kg/m3 | 333.15 | Densiti... |
| ρl | 658.16 | kg/m3 | 333.15 | Density... |
| ρl | 658.19 | kg/m3 | 333.15 | Advance... |
| ρl | 653.81 | kg/m3 | 338.15 | Advance... |
| ρl | 653.80 | kg/m3 | 338.15 | Density... |
| ρl | 649.40 | kg/m3 | 343.15 | Density... |
| ρl | 649.44 | kg/m3 | 343.15 | Densiti... |
| ρl | 649.40 | kg/m3 | 343.15 | Advance... |
| ΔfusS | [54.70; 55.56] | J/mol×K | [165.30; 165.79] |
|
| ΔfusS | 54.70 | J/mol×K | 165.30 | NIST |
| ΔfusS | 55.56 | J/mol×K | 165.79 | NIST |
| csound,fluid | [979.25; 1124.31] | m/s | [288.15; 323.15] |
|
|
T(K) Speed of sound in fluid (m/s) 980 1000 1020 1040 1060 1080 1100 1120 290 300 310 320 | ||||
| csound,fluid | 1124.31 | m/s | 288.15 | Tempera... |
| csound,fluid | 1124.31 | m/s | 288.15 | Influen... |
| csound,fluid | 1113.83 | m/s | 290.65 | Influen... |
| csound,fluid | 1103.30 | m/s | 293.15 | Influen... |
| csound,fluid | 1092.66 | m/s | 295.65 | Influen... |
| csound,fluid | 1082.20 | m/s | 298.15 | Influen... |
| csound,fluid | 1082.20 | m/s | 298.15 | Tempera... |
| csound,fluid | 1071.72 | m/s | 300.65 | Influen... |
| csound,fluid | 1061.30 | m/s | 303.15 | Influen... |
| csound,fluid | 1050.89 | m/s | 305.65 | Influen... |
| csound,fluid | 1040.53 | m/s | 308.15 | Influen... |
| csound,fluid | 1030.22 | m/s | 310.65 | Influen... |
| csound,fluid | 1019.94 | m/s | 313.15 | Influen... |
| csound,fluid | 1009.71 | m/s | 315.65 | Influen... |
| csound,fluid | 999.53 | m/s | 318.15 | Influen... |
| csound,fluid | 989.37 | m/s | 320.65 | Influen... |
| csound,fluid | 979.25 | m/s | 323.15 | Influen... |
| csound,fluid | 979.25 | m/s | 323.15 | Tempera... |
| γ | [0.02; 0.02] | N/m | [288.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.02 290 300 310 320 | ||||
| γ | 0.02 | N/m | 288.15 | Densiti... |
| γ | 0.02 | N/m | 288.15 | Surface... |
| γ | 0.02 | N/m | 288.15 | Densiti... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | Densiti... |
| γ | 0.02 | N/m | 298.15 | Densiti... |
| γ | 0.02 | N/m | 298.20 | KDB |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Densiti... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Densiti... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| λ | [0.09; 0.10] | W/m×K | [259.11; 328.14] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.09 0.1 0.1 0.11 260 280 300 320 | ||||
| λ | 0.10 | W/m×K | 259.11 | Thermal... |
| λ | 0.10 | W/m×K | 259.32 | Thermal... |
| λ | 0.10 | W/m×K | 259.52 | Thermal... |
| λ | 0.10 | W/m×K | 277.52 | Thermal... |
| λ | 0.10 | W/m×K | 277.74 | Thermal... |
| λ | 0.10 | W/m×K | 277.93 | Thermal... |
| λ | 0.10 | W/m×K | 295.67 | Thermal... |
| λ | 0.10 | W/m×K | 295.90 | Thermal... |
| λ | 0.10 | W/m×K | 296.10 | Thermal... |
| λ | 0.09 | W/m×K | 313.79 | Thermal... |
| λ | 0.09 | W/m×K | 314.02 | Thermal... |
| λ | 0.09 | W/m×K | 314.22 | Thermal... |
| λ | 0.09 | W/m×K | 327.69 | Thermal... |
| λ | 0.09 | W/m×K | 327.93 | Thermal... |
| λ | 0.09 | W/m×K | 328.14 | Thermal... |
Datasets
- Viscosity, Pa*s (2)
- Refractive index (Na D-line) (1)
- Mass density, kg/m3 (1)
- Speed of sound, m/s (2)
- Thermal conductivity, W/m/K (1)
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 293.15 | 100.00 | 0.0005 |
| 293.15 | 1000.00 | 0.0005 |
| 293.15 | 5000.00 | 0.0005 |
| 293.15 | 10000.00 | 0.0006 |
| 293.15 | 20000.00 | 0.0006 |
| 293.15 | 30000.00 | 0.0007 |
| 293.15 | 40000.00 | 0.0008 |
| 293.15 | 50000.00 | 0.0009 |
| 293.15 | 60000.00 | 0.0010 |
| 293.15 | 70000.00 | 0.0010 |
| 293.15 | 80000.00 | 0.0011 |
| 293.15 | 100000.00 | 0.0013 |
| 293.15 | 120000.00 | 0.0015 |
| 293.15 | 140000.00 | 0.0017 |
| 298.15 | 100.00 | 0.0005 |
| 298.15 | 1000.00 | 0.0005 |
| 298.15 | 5000.00 | 0.0005 |
| 298.15 | 10000.00 | 0.0005 |
| 298.15 | 20000.00 | 0.0006 |
| 298.15 | 30000.00 | 0.0007 |
| 298.15 | 40000.00 | 0.0007 |
| 298.15 | 50000.00 | 0.0008 |
| 298.15 | 60000.00 | 0.0009 |
| 298.15 | 70000.00 | 0.0010 |
| 298.15 | 80000.00 | 0.0011 |
| 298.15 | 100000.00 | 0.0012 |
| 298.15 | 120000.00 | 0.0014 |
| 298.15 | 140000.00 | 0.0016 |
| 313.15 | 100.00 | 0.0004 |
| 313.15 | 1000.00 | 0.0004 |
| 313.15 | 5000.00 | 0.0004 |
| 313.15 | 10000.00 | 0.0005 |
| 313.15 | 20000.00 | 0.0005 |
| 313.15 | 30000.00 | 0.0006 |
| 313.15 | 40000.00 | 0.0006 |
| 313.15 | 50000.00 | 0.0007 |
| 313.15 | 60000.00 | 0.0008 |
| 313.15 | 70000.00 | 0.0008 |
| 313.15 | 80000.00 | 0.0009 |
| 313.15 | 100000.00 | 0.0010 |
| 313.15 | 120000.00 | 0.0012 |
| 313.15 | 140000.00 | 0.0014 |
| 323.15 | 100.00 | 0.0004 |
| 323.15 | 1000.00 | 0.0004 |
| 323.15 | 5000.00 | 0.0004 |
| 323.15 | 10000.00 | 0.0004 |
| 323.15 | 20000.00 | 0.0005 |
| 323.15 | 30000.00 | 0.0005 |
| 323.15 | 40000.00 | 0.0006 |
| 323.15 | 50000.00 | 0.0006 |
| 323.15 | 60000.00 | 0.0007 |
| 323.15 | 70000.00 | 0.0007 |
| 323.15 | 80000.00 | 0.0008 |
| 323.15 | 100000.00 | 0.0009 |
| 323.15 | 120000.00 | 0.0011 |
| 323.15 | 140000.00 | 0.0012 |
| 333.15 | 100.00 | 0.0003 |
| 333.15 | 1000.00 | 0.0003 |
| 333.15 | 5000.00 | 0.0004 |
| 333.15 | 10000.00 | 0.0004 |
| 333.15 | 20000.00 | 0.0004 |
| 333.15 | 30000.00 | 0.0005 |
| 333.15 | 40000.00 | 0.0005 |
| 333.15 | 50000.00 | 0.0006 |
| 333.15 | 60000.00 | 0.0006 |
| 333.15 | 70000.00 | 0.0007 |
| 333.15 | 80000.00 | 0.0007 |
| 333.15 | 100000.00 | 0.0008 |
| 333.15 | 120000.00 | 0.0010 |
| 333.15 | 140000.00 | 0.0011 |
| 348.15 | 100.00 | 0.0003 |
| 348.15 | 1000.00 | 0.0003 |
| 348.15 | 5000.00 | 0.0003 |
| 348.15 | 10000.00 | 0.0003 |
| 348.15 | 20000.00 | 0.0004 |
| 348.15 | 30000.00 | 0.0004 |
| 348.15 | 40000.00 | 0.0005 |
| 348.15 | 50000.00 | 0.0005 |
| 348.15 | 60000.00 | 0.0005 |
| 348.15 | 70000.00 | 0.0006 |
| 348.15 | 80000.00 | 0.0007 |
| 348.15 | 100000.00 | 0.0008 |
| 348.15 | 120000.00 | 0.0009 |
| 348.15 | 140000.00 | 0.0010 |
| 353.15 | 100.00 | 0.0003 |
| 353.15 | 1000.00 | 0.0003 |
| 353.15 | 5000.00 | 0.0003 |
| 353.15 | 10000.00 | 0.0003 |
| 353.15 | 20000.00 | 0.0004 |
| 353.15 | 30000.00 | 0.0004 |
| 353.15 | 40000.00 | 0.0004 |
| 353.15 | 50000.00 | 0.0005 |
| 353.15 | 60000.00 | 0.0005 |
| 353.15 | 70000.00 | 0.0006 |
| 353.15 | 80000.00 | 0.0006 |
| 353.15 | 100000.00 | 0.0007 |
| 353.15 | 120000.00 | 0.0008 |
| 353.15 | 140000.00 | 0.0009 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0005 |
| Reference | ||
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Refractive index (Na D-line) - Liquid |
| 298.15 | 101.33 | 1.3891 |
| 293.15 | 101.00 | 1.4211 |
| 303.15 | 101.00 | 1.416 |
| 313.15 | 101.00 | 1.4109 |
| 323.15 | 101.00 | 1.4055 |
| 293.15 | 101.00 | 1.3916 |
| 303.15 | 101.00 | 1.3866 |
| 313.15 | 101.00 | 1.3814 |
| 323.15 | 101.00 | 1.3763 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 687.32 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 294.06 | 100.00 | 1099.7 |
| 304.03 | 100.00 | 1058.5 |
| 313.81 | 100.00 | 1017.3 |
| 323.56 | 100.00 | 978.2 |
| 333.42 | 100.00 | 938.5 |
| 342.88 | 100.00 | 898.0 |
| 352.86 | 100.00 | 858.9 |
| 363.55 | 100.00 | 821.9 |
| 294.37 | 3000.00 | 1127.4 |
| 304.16 | 3000.00 | 1088.2 |
| 313.92 | 3000.00 | 1037.2 |
| 323.61 | 3000.00 | 999.1 |
| 333.48 | 3000.00 | 968.0 |
| 343.07 | 3000.00 | 927.9 |
| 352.89 | 3000.00 | 891.7 |
| 363.39 | 3000.00 | 852.2 |
| 373.04 | 3000.00 | 821.1 |
| 383.18 | 3000.00 | 783.2 |
| 393.83 | 3000.00 | 742.3 |
| 402.16 | 3000.00 | 716.5 |
| 412.57 | 3000.00 | 677.6 |
| 423.95 | 3000.00 | 636.8 |
| 434.51 | 3000.00 | 602.6 |
| 443.70 | 3000.00 | 569.7 |
| 452.94 | 3000.00 | 538.4 |
| 462.54 | 3000.00 | 502.1 |
| 472.45 | 3000.00 | 464.2 |
| 483.15 | 3000.00 | 423.5 |
| 493.12 | 3000.00 | 386.4 |
| 502.80 | 3000.00 | 350.1 |
| 512.41 | 3000.00 | 311.4 |
| 523.31 | 3000.00 | 264.5 |
| 294.65 | 6000.00 | 1147.6 |
| 304.23 | 6000.00 | 1109.6 |
| 313.96 | 6000.00 | 1065.2 |
| 323.65 | 6000.00 | 1027.4 |
| 333.50 | 6000.00 | 996.0 |
| 343.16 | 6000.00 | 954.8 |
| 352.94 | 6000.00 | 921.1 |
| 363.49 | 6000.00 | 883.5 |
| 373.27 | 6000.00 | 843.9 |
| 383.80 | 6000.00 | 813.8 |
| 394.00 | 6000.00 | 782.2 |
| 402.48 | 6000.00 | 750.9 |
| 412.84 | 6000.00 | 719.3 |
| 424.32 | 6000.00 | 678.1 |
| 434.94 | 6000.00 | 647.4 |
| 444.00 | 6000.00 | 619.6 |
| 453.22 | 6000.00 | 588.3 |
| 463.04 | 6000.00 | 558.9 |
| 472.86 | 6000.00 | 530.7 |
| 483.63 | 6000.00 | 496.7 |
| 493.56 | 6000.00 | 464.9 |
| 503.17 | 6000.00 | 435.4 |
| 513.04 | 6000.00 | 404.0 |
| 523.97 | 6000.00 | 371.4 |
| 294.84 | 10000.00 | 1176.1 |
| 304.27 | 10000.00 | 1136.9 |
| 313.82 | 10000.00 | 1100.1 |
| 323.67 | 10000.00 | 1060.4 |
| 333.46 | 10000.00 | 1028.0 |
| 343.22 | 10000.00 | 990.3 |
| 353.01 | 10000.00 | 961.7 |
| 363.54 | 10000.00 | 925.7 |
| 373.41 | 10000.00 | 888.2 |
| 384.11 | 10000.00 | 855.6 |
| 394.15 | 10000.00 | 825.8 |
| 402.64 | 10000.00 | 800.2 |
| 413.07 | 10000.00 | 766.7 |
| 424.49 | 10000.00 | 732.1 |
| 435.26 | 10000.00 | 701.0 |
| 444.22 | 10000.00 | 677.1 |
| 454.37 | 10000.00 | 648.8 |
| 463.43 | 10000.00 | 622.7 |
| 473.22 | 10000.00 | 596.3 |
| 484.05 | 10000.00 | 569.9 |
| 494.09 | 10000.00 | 542.2 |
| 503.79 | 10000.00 | 516.1 |
| 513.78 | 10000.00 | 491.8 |
| 524.59 | 10000.00 | 463.0 |
| 294.97 | 12000.00 | 1181.7 |
| 304.27 | 12000.00 | 1147.7 |
| 313.85 | 12000.00 | 1110.8 |
| 323.71 | 12000.00 | 1075.4 |
| 333.40 | 12000.00 | 1041.9 |
| 343.21 | 12000.00 | 1008.5 |
| 353.04 | 12000.00 | 975.5 |
| 363.58 | 12000.00 | 943.8 |
| 373.49 | 12000.00 | 908.6 |
| 384.26 | 12000.00 | 876.5 |
| 394.19 | 12000.00 | 848.1 |
| 402.78 | 12000.00 | 819.5 |
| 413.22 | 12000.00 | 791.3 |
| 424.59 | 12000.00 | 756.7 |
| 435.36 | 12000.00 | 726.5 |
| 444.36 | 12000.00 | 700.3 |
| 455.24 | 12000.00 | 671.1 |
| 463.72 | 12000.00 | 651.6 |
| 473.48 | 12000.00 | 627.7 |
| 484.30 | 12000.00 | 598.4 |
| 494.42 | 12000.00 | 576.5 |
| 504.09 | 12000.00 | 550.4 |
| 514.01 | 12000.00 | 526.6 |
| 524.70 | 12000.00 | 501.3 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 100.00 | 293.15 | 1104.6 |
| 100.00 | 303.15 | 1061.7 |
| 100.00 | 313.15 | 1019.1 |
| 100.00 | 323.15 | 977.9 |
| 100.00 | 333.15 | 935.8 |
| 100.00 | 343.15 | 897.3 |
| 100.00 | 353.15 | 858.2 |
| 100.00 | 363.15 | 817.2 |
| 100.00 | 373.15 | 780.4 |
| 10000.00 | 293.15 | 1178.5 |
| 10000.00 | 303.15 | 1139.3 |
| 10000.00 | 313.15 | 1100.9 |
| 10000.00 | 323.15 | 1063.5 |
| 10000.00 | 333.15 | 1026.6 |
| 10000.00 | 343.15 | 992.6 |
| 10000.00 | 353.15 | 958.0 |
| 10000.00 | 363.15 | 924.3 |
| 10000.00 | 373.15 | 891.0 |
| 20000.00 | 293.15 | 1244.6 |
| 20000.00 | 303.15 | 1208.6 |
| 20000.00 | 313.15 | 1173.0 |
| 20000.00 | 323.15 | 1138.8 |
| 20000.00 | 333.15 | 1105.2 |
| 20000.00 | 343.15 | 1071.6 |
| 20000.00 | 353.15 | 1041.7 |
| 20000.00 | 363.15 | 1011.1 |
| 20000.00 | 373.15 | 980.7 |
| 30000.00 | 293.15 | 1304.8 |
| 30000.00 | 303.15 | 1270.2 |
| 30000.00 | 313.15 | 1237.0 |
| 30000.00 | 323.15 | 1204.7 |
| 30000.00 | 333.15 | 1173.0 |
| 30000.00 | 343.15 | 1142.7 |
| 30000.00 | 353.15 | 1114.1 |
| 30000.00 | 363.15 | 1085.5 |
| 30000.00 | 373.15 | 1057.5 |
| 40000.00 | 293.15 | 1358.5 |
| 40000.00 | 303.15 | 1326.8 |
| 40000.00 | 313.15 | 1295.2 |
| 40000.00 | 323.15 | 1264.6 |
| 40000.00 | 333.15 | 1234.2 |
| 40000.00 | 343.15 | 1205.7 |
| 40000.00 | 353.15 | 1178.7 |
| 40000.00 | 363.15 | 1151.4 |
| 40000.00 | 373.15 | 1125.2 |
| 50000.00 | 293.15 | 1410.3 |
| 50000.00 | 303.15 | 1378.5 |
| 50000.00 | 313.15 | 1349.3 |
| 50000.00 | 323.15 | 1319.0 |
| 50000.00 | 333.15 | 1290.2 |
| 50000.00 | 343.15 | 1262.9 |
| 50000.00 | 353.15 | 1236.1 |
| 50000.00 | 363.15 | 1211.3 |
| 50000.00 | 373.15 | 1185.9 |
| 60000.00 | 293.15 | 1458.1 |
| 60000.00 | 303.15 | 1427.0 |
| 60000.00 | 313.15 | 1397.6 |
| 60000.00 | 323.15 | 1369.8 |
| 60000.00 | 333.15 | 1341.8 |
| 60000.00 | 343.15 | 1315.4 |
| 60000.00 | 353.15 | 1290.4 |
| 60000.00 | 363.15 | 1265.7 |
| 60000.00 | 373.15 | 1242.1 |
| 70000.00 | 293.15 | 1502.5 |
| 70000.00 | 303.15 | 1472.6 |
| 70000.00 | 313.15 | 1443.4 |
| 70000.00 | 323.15 | 1416.6 |
| 70000.00 | 333.15 | 1390.0 |
| 70000.00 | 343.15 | 1363.5 |
| 70000.00 | 353.15 | 1339.5 |
| 70000.00 | 363.15 | 1316.6 |
| 70000.00 | 373.15 | 1293.1 |
| 80000.00 | 293.15 | 1544.7 |
| 80000.00 | 303.15 | 1515.6 |
| 80000.00 | 313.15 | 1487.6 |
| 80000.00 | 323.15 | 1461.2 |
| 80000.00 | 333.15 | 1434.9 |
| 80000.00 | 343.15 | 1410.8 |
| 80000.00 | 353.15 | 1386.8 |
| 80000.00 | 363.15 | 1364.4 |
| 80000.00 | 373.15 | 1341.5 |
| 90000.00 | 293.15 | 1584.5 |
| 90000.00 | 303.15 | 1556.4 |
| 90000.00 | 313.15 | 1529.0 |
| 90000.00 | 323.15 | 1503.4 |
| 90000.00 | 333.15 | 1479.0 |
| 90000.00 | 343.15 | 1453.6 |
| 90000.00 | 353.15 | 1431.0 |
| 90000.00 | 363.15 | 1408.2 |
| 90000.00 | 373.15 | 1386.0 |
| 100000.00 | 293.15 | 1622.6 |
| 100000.00 | 303.15 | 1594.5 |
| 100000.00 | 313.15 | 1568.7 |
| 100000.00 | 323.15 | 1543.4 |
| 100000.00 | 333.15 | 1519.0 |
| 100000.00 | 343.15 | 1495.3 |
| 100000.00 | 353.15 | 1472.5 |
| 100000.00 | 363.15 | 1449.9 |
| 100000.00 | 373.15 | 1428.5 |
| 110000.00 | 293.15 | 1658.9 |
| 110000.00 | 303.15 | 1632.1 |
| 110000.00 | 313.15 | 1605.9 |
| 110000.00 | 323.15 | 1581.4 |
| 110000.00 | 333.15 | 1557.7 |
| 110000.00 | 343.15 | 1534.0 |
| 110000.00 | 353.15 | 1512.1 |
| 110000.00 | 363.15 | 1490.6 |
| 110000.00 | 373.15 | 1469.2 |
| 120000.00 | 293.15 | 1694.0 |
| 120000.00 | 303.15 | 1667.5 |
| 120000.00 | 313.15 | 1641.7 |
| 120000.00 | 323.15 | 1617.8 |
| 120000.00 | 333.15 | 1594.1 |
| 120000.00 | 343.15 | 1571.7 |
| 120000.00 | 353.15 | 1549.6 |
| 120000.00 | 363.15 | 1529.0 |
| 120000.00 | 373.15 | 1508.2 |
| 130000.00 | 293.15 | 1727.5 |
| 130000.00 | 303.15 | 1701.6 |
| 130000.00 | 313.15 | 1676.3 |
| 130000.00 | 323.15 | 1653.1 |
| 130000.00 | 333.15 | 1629.5 |
| 130000.00 | 343.15 | 1607.2 |
| 130000.00 | 353.15 | 1585.9 |
| 130000.00 | 363.15 | 1565.5 |
| 130000.00 | 373.15 | 1545.1 |
| 140000.00 | 293.15 | 1760.1 |
| 140000.00 | 303.15 | 1734.3 |
| 140000.00 | 313.15 | 1709.4 |
| 140000.00 | 323.15 | 1686.4 |
| 140000.00 | 333.15 | 1663.5 |
| 140000.00 | 343.15 | 1641.7 |
| 140000.00 | 353.15 | 1620.5 |
| 140000.00 | 363.15 | 1600.8 |
| 140000.00 | 373.15 | 1580.3 |
| 150000.00 | 293.15 | 1791.1 |
| 150000.00 | 303.15 | 1766.4 |
| 150000.00 | 313.15 | 1741.7 |
| 150000.00 | 323.15 | 1718.6 |
| 150000.00 | 333.15 | 1696.2 |
| 150000.00 | 343.15 | 1675.0 |
| 150000.00 | 353.15 | 1654.1 |
| 150000.00 | 363.15 | 1634.2 |
| 150000.00 | 373.15 | 1614.0 |
| Reference | ||
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 254.60 | 100.00 | 0.1047 |
| 254.51 | 5000.00 | 0.1066 |
| 254.67 | 10100.00 | 0.1088 |
| 254.77 | 20000.00 | 0.1121 |
| 254.73 | 30000.00 | 0.1157 |
| 274.66 | 100.00 | 0.1004 |
| 274.63 | 5000.00 | 0.1021 |
| 274.61 | 10000.00 | 0.1041 |
| 274.61 | 20000.00 | 0.1080 |
| 274.57 | 30000.00 | 0.1114 |
| 295.33 | 100.00 | 0.0959 |
| 295.22 | 5000.00 | 0.0979 |
| 295.22 | 10100.00 | 0.1003 |
| 295.06 | 20100.00 | 0.1042 |
| 295.04 | 30100.00 | 0.1083 |
| 314.99 | 100.00 | 0.0907 |
| 314.85 | 5000.00 | 0.0930 |
| 314.87 | 10000.00 | 0.0953 |
| 314.93 | 20000.00 | 0.0996 |
| 314.91 | 29900.00 | 0.1038 |
| 334.53 | 100.00 | 0.0859 |
| 334.49 | 5100.00 | 0.0886 |
| 334.56 | 10000.00 | 0.0908 |
| 334.62 | 20000.00 | 0.0958 |
| 334.59 | 30000.00 | 0.0999 |
| 354.50 | 200.00 | 0.0817 |
| 354.78 | 5100.00 | 0.0843 |
| 354.83 | 10000.00 | 0.0868 |
| 354.73 | 20000.00 | 0.0915 |
| 354.80 | 30000.00 | 0.0960 |
| 374.63 | 400.00 | 0.0784 |
| 374.61 | 5000.00 | 0.0807 |
| 374.18 | 10000.00 | 0.0830 |
| 374.21 | 19900.00 | 0.0875 |
| 374.25 | 29900.00 | 0.0925 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [268.57; 398.53] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40806e+01 | |||
| Coefficient B | -3.12864e+03 | |||
| Coefficient C | -4.17450e+01 | |||
| Temperature range, min. | 268.57 | |||
| Temperature range, max. | 398.53 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
| Pvap | 1.33 | kPa | 268.57 | Calculated Property |
| Pvap | 3.04 | kPa | 283.01 | Calculated Property |
| Pvap | 6.33 | kPa | 297.45 | Calculated Property |
| Pvap | 12.17 | kPa | 311.89 | Calculated Property |
| Pvap | 21.91 | kPa | 326.33 | Calculated Property |
| Pvap | 37.25 | kPa | 340.77 | Calculated Property |
| Pvap | 60.32 | kPa | 355.21 | Calculated Property |
| Pvap | 93.62 | kPa | 369.65 | Calculated Property |
| Pvap | 140.01 | kPa | 384.09 | Calculated Property |
| Pvap | 202.67 | kPa | 398.53 | Calculated Property |
| Pvap | [1.48e-05; 2584.81] | kPa | [165.78; 543.96] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.67458e+01 | |||
| Coefficient B | -7.04177e+03 | |||
| Coefficient C | -1.08858e+01 | |||
| Coefficient D | 8.87277e-06 | |||
| Temperature range, min. | 165.78 | |||
| Temperature range, max. | 543.96 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 200 300 400 500 | ||||
| Pvap | 1.48e-05 | kPa | 165.78 | Calculated Property |
| Pvap | 7.82e-03 | kPa | 207.80 | Calculated Property |
| Pvap | 0.37 | kPa | 249.82 | Calculated Property |
| Pvap | 4.87 | kPa | 291.84 | Calculated Property |
| Pvap | 29.62 | kPa | 333.86 | Calculated Property |
| Pvap | 112.21 | kPa | 375.88 | Calculated Property |
| Pvap | 313.08 | kPa | 417.90 | Calculated Property |
| Pvap | 713.56 | kPa | 459.92 | Calculated Property |
| Pvap | 1420.70 | kPa | 501.94 | Calculated Property |
| Pvap | 2584.81 | kPa | 543.96 | Calculated Property |
Similar Compounds
Find more compounds similar to Pentane, 2,2,4-trimethyl-.
Mixtures
- Propane, 2-methoxy-2-methyl- + Pentane, 2,2,4-trimethyl-
- Diisopropyl ether + Pentane, 2,2,4-trimethyl-
- Methylal + Pentane, 2,2,4-trimethyl-
- Acetone + Pentane, 2,2,4-trimethyl-
- Ethanol + Pentane, 2,2,4-trimethyl-
- Ethanol + Acetone + Pentane, 2,2,4-trimethyl-
- Diisopropyl ether + Ethanol + Pentane, 2,2,4-trimethyl-
- 2-Butanone + Pentane, 2,2,4-trimethyl-
- 2-Butanone + Ethanol + Pentane, 2,2,4-trimethyl-
- Thiophene + Pentane, 2,2,4-trimethyl-
- 2-Butanone, 3-methyl- + Pentane, 2,2,4-trimethyl-
- Isopropyl Alcohol + Pentane, 2,2,4-trimethyl-
- 2-Butanone, 3-methyl- + Isopropyl Alcohol + Pentane, 2,2,4-trimethyl-
- 2-Pyrrolidinone, 1-methyl- + Pentane, 2,2,4-trimethyl-
- Carbonic acid, dimethyl ester + Pentane, 2,2,4-trimethyl-
- Carbonic acid, dimethyl ester + Ethanol + Pentane, 2,2,4-trimethyl-
- Thiophene, 3-methyl- + Pentane, 2,2,4-trimethyl-
- 1-Butanethiol + Pentane, 2,2,4-trimethyl-
- Disulfide, dimethyl + Pentane, 2,2,4-trimethyl-
- Diethyl disulfide + Pentane, 2,2,4-trimethyl-
Find more mixtures with Pentane, 2,2,4-trimethyl-.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
- Liquid liquid equilibria for pseudoternary systems: isooctane benzene (methanol +water)
- Phase equilibria for binary systems of octane boosters with 2,2,4-trimethylpentane
- Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
- Solubility of CO2 in branched alkanes in order to extend the PPR78 model (predictive 1978, Peng Robinson EOS with temperature-dependent kij calculated through a group contribution method) to such systems
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Vapor liquid equilibria for binary and ternary mixtures of diisopropyl ether, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
- Vapor liquid equilibria for binary and ternary mixtures of ethanol, 2-butanone, and 2,2,4-trimethylpentane at 101.3 kPa
- Vapor liquid equilibrium for binary system of thiophene + 2,2,4-trimethylpentane at 343.15 and 353.15K and thiophene + 2-ethoxy-2-methylpropane at 333.15 and 343.15K
- Isothermal vapor liquid equilibrium at 303.15K and excess molar volumes at 298.15 K for the ternary system of propyl vinyl ether + 1-propanol + 2,2,4-trimethyl-pentane and its binary sub-systems
- Isothermal vapour liquid equilibria in the binary and ternary systems composed of 2-propanol, 3-methyl-2-butanone and 2,2,4-trimethylpentane
- Measurement and prediction of pyrene solubility in pure, binary, ternary and quaternary solvent systems
- Liquid liquid equilibria of lactam containing binary systems
- Solubility of hydrocarbons in water: Experimental measurements and modeling using a group contribution with association equation of state (GCA-EoS)
- Isothermal vapor liquid equilibrium at 333.15K and excess molar volumes and refractive indices at 298.15K for the mixtures of di-methyl carbonate, ethanol and 2,2,4-trimethylpentane
- Phase equilibria on four binary systems containing 3-methylthiophene
- Isothermal vapor liquid equilibrium at 333.15K, excess molar volumes and refractive indices at 298.15K for mixtures of tert-amyl methyl ether + ethanol + 2,2,4-trimethylpentane
- (Liquid + liquid) equilibria of the quaternary sysytem methanol + isooctane + cyclohexane + benzene at T = 303.15 K
- Excess enthalpies of oxygenated compounds + hydrocarbon mixtures: Binary and ternary mixtures containing dibutyl ether (DBE), 1-butanol and 2,2,4-trimethylpentane at 298.15 K
- Phase equilibrium for the systems diisopropyl ether, isopropyl alcohol + 2,2,4-trimethylpentane and + n-heptane at 101.3 kPa
- Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
- Phase equilibria on five binary systems containing 1-butanethiol and 3-methylthiophene in hydrocarbons
- Phase equilibria for systems containing dimethyl disulfide and diethyl disulfide with hydrocarbons at 368.15 K
- Vapor liquid equilibrium for binary system of tetrahydrothiophene + 2,2,4-trimethylpentane and tetrahydrothiophene + 2,4,4-trimethyl-1-pentene at 358.15 and 368.15 K
- Infinite dilution activity coefficient and vapour liquid equilibrium measurements for dimethylsulphide and tetrahydrothiophene with hydrocarbons
- Volumetric behavior of the binary systems benzene + cyclohexane and benzene + 2,2,4-trimethyl-pentane at temperatures 293.15-323.15K
- Measurements and correlation of vapour liquid equilibria of 2-butanone and hydrocarbons binary systems at two different pressures
- Isothermal vapour-liquid equilibria in the binary and ternary systems composed of 2,2,4-trimethylpentane, 2-methyl-1-propanol, and 4-methyl-2-pentanone
- 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
- Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- (Liquid + liquid) equilibria for the ternary system of (N-formylmorpholine + ethylbenzene + 2,2,4-trimethylpentane) at temperatures (303.15, 313.15, and 323.15) K
- Excess molar volumes, excess molar enthalpies and refractive index deviations for binary mixtures of propan-1-ol, butan-1-ol and pentan-1-ol with 2,2,4-trimethylpentane at 298.15 K
- Volumetric behavior of the ternary system benzene-2-methoxy-2-methylbutane-2,2,4-trimethylpentane and all binary sub-systems at temperature range (298.15 - 318.15) K
- Vapour liquid equilibria and excess enthalpies of the binary mixtures 1-pentanol with 2,2,4-trimethylpentane or n-heptane
- The liquid-liquid coexistence curves of {x nitrobenzene + (1 - x) 2-methylpentane} and {x nitrobenzene + (1 - x) isooctane} in the critical region
- Towards automated characterisation of liquid-liquid equilibria
- Phase equilibrium properties of binary and ternary mixtures containing 2-butanol, 2,2,4- trimethylpentane and 1-hexene at 313.15 K
- Thermodynamic behaviour of second generation biofuels: Vapour liquid equilibria and excess enthalpies of the binary mixtures 2-pentanol and n-heptane or 2,2,4-trimethylpentane
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- High-pressure vapor-liquid equilibria of the second generation biofuel blends (2-methylfuran + iso-octane) and (2-methyltetrahydrofuran + di-n-butyl ether): Experiments and PCP-SAFT modeling
- Vapour-liquid equilibria of the ternary mixture (1-pentanol + 2,2,4-trimethylpentane + heptane) and the binary mixture (2,2,4-trimethylpentane + heptane) at T = 313.15 K for the characterization of second generation biofuels.
- Liquid-liquid equilibria in the ternary and multicomponent systems involving hydrocarbons, thiophene or pyridine and ionic liquid (1-benzyl-3-metylimidazolium bis(trifluorometylsulfonyl)imide)
- 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
- Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
- A milliliter-scale setup for the efficient characterization of isothermal vapor-liquid equilibria using Raman spectroscopy
- 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
- Isobaric vapor-liquid equilibrium, density and speed of sound of binary mixtures 2,2,4-trimethylpentane + 1-butanol or dibutyl ether (DBE) 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
- The pressure dependence of viscosity for 2,2,4 trimethylhexane to 1 GPa along the 20 C isotherm
- Excess enthalpies of binary mixtures of 1-hexene with some branched alkanes at the temperature 298.15 K
- 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
- Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
- (Vapor + liquid) equilibria of binary mixtures formed by iso-octane with a variety of compounds at 95.8 kPa
- Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
- Volumetric behaviour of binary liquid systems composed of toluene, isooctane, and methyl tert-butyl ether at temperatures from (298.15 to 328.15) K
- Evaluation of the polysubstituted pyridinium ionic liquid [hmmpy][Ntf2] as a suitable solvent for desulfurization: Phase equilibria
- Volumetric behaviour of the ternary liquid system composed of methyl tert-butyl ether, toluene, and isooctane at temperatures from (298.15 to 328.15) K: Experimental data and correlation
- Densities, viscosities, refractive indices, and surface tensions for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- Volumetric behaviour of binary and ternary liquid systems composed of ethanol, isooctane, and toluene at temperatures from (298.15 to 328.15) K. Experimental data and correlation
- Isothermal (vapour + liquid) equilibria in the binary and ternary systems composed of 2-propanol, 2,2,4-trimethylpentane, and 2,4-dimethyl-3-pentanone
- (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
- (Vapour + liquid) equilibria for binary and ternary mixtures of 2-propanol, tetrahydropyran, and 2,2,4-trimethylpentane at P = 101.3 kPa
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- The potential of head-space gas chromatography for VLE measurements
- 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
- Densities and viscosities of binary and ternary mixtures of cyclohexanone, 1,4-dioxane and isooctane from T = (288.15 to 313.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- 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
- Advanced calibration, adjustment, and operation of a density and sound speed analyzer
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- 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
- Vapour-liquid equilibria of binary and ternary mixtures containing 1-butanol, 2,2,4-trimethylpentane and 1-hexene at T = 313.15 K
- 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
- Volumetric behaviour of the (2,2,4-trimethylpentane + methylbenzene + butan-1-ol) ternary system and its binary sub-systems within the temperature range (298.15-328.15) K
- 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
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Application of 1-pentyl-3-methylimidazolium bis(trifluoromethylsulfonyl) imide for desulfurization, denitrification and dearomatization of FCC gasoline
- 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
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- Contributing to accurate high pressure viscosity measurements: Vibrating wire viscometer and falling body viscometer techniques
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Viscosities of binary mixtures containing 1-butanol + 2,2,4-trimethylpentane or + 1,2,4-trimethylbenzene at high pressures for the thermophysical characterization of biofuels
- 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 limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Thermodynamics of mixtures containing aromatic nitriles
- 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
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- Viscosities of binary mixtures containing 2-butanol + hydrocarbons (2,2,4-trimethylpentane or 1,2,4-trimethylbenzene) at high pressures for the implementation of second generation biofuels
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Excess volumes, densities, speeds of sound and viscosities for the binary systems of diisopropyl ether with hydrocarbons at 303.15K
- Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
- Densities, Viscosities, Refractive Indices, and Surface Tensions of Binary Mixtures of 2,2,4-Trimethylpentane with Several Alkylated Cyclohexanes from (293.15 to 343.15) K
- A Study on Alkane + Ester + Ester Systems. Physicochemical Behavior of Binaries and Ternaries of Octane or Iso-octane with Methyl Esters (Ethanoate, Butanoate, Pentanoate)
- Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane +1-Alkanols from 298.15 to 323.15 K
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Liquid Liquid Equilibria, Equilibrium Phase Densities, and Refractive Indices for the Quaternary Mixtures Containing 2-Propanol or 2-Methyl-2-Propanol of Fuel Oxygenate at T = 298.15 and 318.15 K
- Solubility of 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
- 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
- Measurement and Correlation of Isothermal Binary Vapor Liquid Equilibrium for Diethyl Carbonate + Isooctane/n-Heptane/Toluene Systems
- High Pressure Volumetric Properties of the Binary Mixtures Di-isopropyl Ether + 2,2,4-Trimethylpentane
- Experimental Solubility Data for Binary Mixtures of Ethane and 2,2,4-Trimethylpentane at Pressures up to 6 MPa Using a New Variable-Volume Sapphire Cell
- Measurements of the Speed of Sound in Liquid and Supercritical n-Octane and Isooctane
- Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
- Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary 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
- Vapor-Liquid Equilibrium Measurements of Ether Alcohol Blends for Investigation on Reformulated Gas
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
- Measurements of the Thermal Conductivity of n-Octane, Isooctane, 1-Octene, and 1-Octanol in the Temperature Range from 253 to 393 K at Pressures up to 30 MPa
- Measurement of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
- Effect of Composition and Temperature upon Density, Viscosity, Surface Tension, and Refractive Index of 2,2,4-Trimethylpentane + Cyclohexane + Decane Ternary Liquid Systems
- Thermal Conductivity and Thermal Diffusivity of Sixteen Isomers of Alkanes: CnH2n+2 (n = 6 to 8)
- Isobaric Vapor-Liquid and Vapor-Liquid-Liquid Equilibria Data for the System Water + Isopropanol + Isooctane
- Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
- Phase Separation in Binary Mixtures Containing Linear Perfluoroalkanes
- Densities and Viscosities for Binary and Ternary Mixtures of Ethanol, 2-Butanone, and 2,2,4-Trimethylpentane at T = (298.15, 308.15, and 318.15) K
- Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
- Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Ethanol, 2-Methylpropan-2-ol, and 2,2,4-Trimethylpentane
- Speed of Sound of 2-Methylpentane, 2,3-Dimethylpentane, and 2,2,4-Trimethylpentane from (293.15 to 373.15) K and up to 150 MPa
- Density, Viscosity, and Speed of Sound of Solutions of AOT Reverse Micelles in 2,2,4-Trimethylpentane
- Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of Diisopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
- Phase Equilibria on Four Binary Systems: 1,2-Dichloroethane + trans-1,2-Dichloroethylene, 1-Octene + 2-Methyl Thiophene, 2-Ethyl Thiophene + 2,2,4-Trimethylpentane, and Cyclopropanecarbonitrile + Water
- (Liquid + Liquid) Equilibria of Oxygenate Fuel Additives with Water: (Water + Diisopropyl Ether + 2,2,4-Trimethylpentane + Ethanol) and (Water + Diisopropyl Ether + 2,2,4-Trimethylpentane + 2-Propanol)
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Vapor-Liquid Equilibrium of Ferrocene in Some Organic Solvents Using Spectroscopic Methods
- Vapor-Liquid Equilibrium of Binary Mixtures. 2. Ethanol + 2,2,4-Trimethylpentane, 1-Butanol + 2,2,4-Trimethylpentane, and Ethanol + o-Xylene
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Density, Speed of Sound, Surface Tension, and Refractive Index of AOT + 2,2,4-Trimethylpentane + Water Mixtures from (5 to 60) deg C
- Excess Molar Volumes at 298.15 K and Isothermal Vapor-Liquid Equilibria at 333.15 K for the Binary Mixtures of Dimethyl Carbonate with Benzene, Toluene, n-Heptane, and Isooctane
- Solubility of Ethylene in 2,2,4-Trimethylpentane at Various Temperatures and Pressures
- Vapor-Liquid Equilibrium for Binary System of Diethyl Sulfide + n-Heptane and Diethyl Sulfide + 2,2,4-Trimethylpentane at (363.15 and 353.15) K
- Solubility of Anthracene in Binary Diisopropyl Ether + Alkane Solvent Mixtures at 298.15 K
- Measurement and Modeling of Liquid-Liquid Equilibrium for Ternary and Quaternary Mixtures of Water, Methanol, 2-Propanol, and 2,2,4-Trimethylpentane at 293.2 K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Solubility of Anthracene and Phenanthrene in Ethanol + 2,2,4-Trimethylpentane Mixtures at Different Temperatures
- 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
- Isothermal Vapor Liquid Equilibrium Data of Propan-1-ol + 2,2,4-Trimethylpentane and Butan-1-ol + 2,2,4-Trimethylpentane at 318.15 K
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Measurement and Calculation of Liquid Liquid Equilibria of Ternary and Quaternary Systems Containing Water, Propan-1-ol, and 2,2,4-Trimethylpentane (TMP) with 2,2'-Oxybis(propane) (DIPE) or Dimethyl Carbonate (DMC)
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Vapor-Liquid Equilibria of Binary Mixtures Containing 1-Butanol and Hydrocarbons at 313.15 K
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Excess Volumes of Ternary Mixtures 2,2,4-Trimethylpentane + Diisopropyl Ether or Methyl tert-Butyl Ether + Methanol, Ethanol, or 1-Propanol at 298.15 K
- 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
- Vapor Liquid Liquid Equilibria Measurements for the Dehydration of Ethanol, Isopropanol, and n-Propanol via Azeotropic Distillation Using DIPE and Isooctane as Entrainers
- Liquid Liquid Equilibria for Dipropylene Glycol Hydrocarbon Binary Systems: Experimental Data and Regression
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
- Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Oxygenated Compounds + Hydrocarbon Mixtures in Fuels and Biofuels: Excess Enthalpies of Ternary Mixtures Containing 1-Butoxybutane + Propan-1-ol +1-Hex-1-ene, or Heptane, or 2,2,4-Trimethylpentane at (298.15 and 313.15) K
- Density, Viscosity, Speed of Sound, Bulk Modulus, and Surface Tension of Binary Mixtures of n-Heptane + 2,2,4-Trimethylpentane at (293.15 to 338.15) K and 0.1 MPa
- Densities and Viscosities of Binary Mixtures of 2,2,4-Trimethylpentane + 1-Propanol, + 1-Pentanol, + 1-Hexanol, and + 1-Heptanol from (298.15 to 323.15) K
- Deduction of Physicochemical Properties from Solubilities: 2,4-Dihydroxybenzophenone, Biotin, and Caprolactam as Examples
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Isothermal Binary and Ternary VLE for the Mixtures of Propyl Vinyl Ether + Ethanol + Isooctane at 323.15 K and VE at 293.15 K
- Critical Temperatures and Pressures of Several Binary and Ternary Mixtures Concerning the Alkylation of 2-Methylpropane with 1-Butene in the Presence of Methane or Carbon Dioxide
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Binary LLE for Propyl Vinyl Ether (PVE) + Water, Ternary LLE for PVE + Methanol or Ethanol + Water at 298.15 K, and VE and centsR at 293.15 K for the Mixture of PVE + Ethanol + 2,2,4-Trimethylpentane
- Isothermal VLE and VE at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether (DIPE) + 1-Propanol + 2,2,4-Trimethylpentane
- Naphthalene Solubility in Binary Solvent Mixtures of 2,2,4-Trimethylpentane + Alcohols at 298.15 K
- Liquid Liquid Equilibrium for Ternary Systems of Propyl Vinyl Ether + C3 or C4 Alcohols + Water at 298.15 K and Excess Molar Enthalpies for Ternary and Constituent Binary Systems of Propyl Vinyl Ether + Ethanol + Isooctane at 303.15 K
- Densities, Viscosities, Refractive Indexes, and Surface Tensions for Binary and Ternary Mixtures of Tetrahydofuran, 2-Propanol, and 2,2,4-Trimethylpentane
- Measurements and Correlation of Liquid Liquid Equilibria of (Water + Ethanol + Dimethyl Carbonate + 2,2,4-Trimethylpentane or n-Heptane) and (Water + Dimethyl Carbonate + n-Heptane + Toluene)
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Solubility of CO2, N2, and CO2 + N2 Gas Mixtures in Isooctane
- Liquid-Liquid Equilibria for [C8mim][NTf2] + Thiophene + 2,2,4-Trimethylpentane or + Toluene
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Densities, Viscosities, Refractive Indices, and Surface Tensions for the Mixtures of 1,3-Dioxolane + 2-Propanol or + 2,2,4-Trimethylpentane at (288.15, 298.15, and 308.15) K and 1,3-Dioxolane + 2-Propanol + 2,2,4-Trimethylpentane at 298.15 K
- Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Molar Volumes, Refractive Indices, and Excess Molar Enthalpies at 303.15 K for the Binary and Ternary Mixtures of Di-isopropyl Ether, Ethanol, and 2,2,4-Trimethylpentane
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibria for Monoethylene Glycol + Hexane and 2,2,4-Trimethylpentane, Water + Hexane and 2,2,4-Trimethylpentane, Monoethylene Glycol + Water + Hexane, and Monoethylene Glycol + Water + 2,2,4-Trimethylpentane in the Temperature Range between T = 283.15 K and T = 323.15 K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Vapor-Liquid Equilibria for Binary and Ternary Mixtures of 1,3-Dioxolane, 2-Propanol, and 2,2,4-Trimethylpentane at 101.3 kPa
- Comparison of the Efficiencies of Amine Extractants on Lactic Acid with Different Organic Solvents
- Isothermal Vapor-Liquid Equilibrium at 333.15 K and Excess Volumes and Molar Refractivity Deviation at 298.15 K for Binary System Dibutyl Ether (DBE) + 2,2,4-Trimethylpentane and for Ternary System DBE + Ethanol + 2,2,4-Trimethylpentane
- Isobaric Vapor-Liquid-Liquid Equilibrium and Vapor-Liquid Equilibrium for the Quaternary System Water-Ethanol-Cyclohexane-Isooctane at 101.3 kPa
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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