- InChI
- InChI=1S/C7H14/c1-3-5-7-6-4-2/h3H,1,4-7H2,2H3
- InChI Key
- ZGEGCLOFRBLKSE-UHFFFAOYSA-N
- Formula
- C7H14
- SMILES
- C=CCCCCC
- Molecular Weight1
- 98.19
- CAS
- 592-76-7
- Other Names
-
- 1-C7H14
- 1-n-Heptene
- HEPTYLENE
- N-HEPT-1-ENE
- NSC 74130
- hept-1-ene
- heptene-1
- «alpha»-Heptylene
- «alpha»-Heptylene
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- AP : Aniline Point (K).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- 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).
- 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 | 0.3580 | KDB | |
| Tig | 533.15 | K | KDB |
| AP | 300.350 | K | KDB |
| ΔcH°liquid | [-4658.30; -4650.98] | kJ/mol |
|
| ΔcH°liquid | -4657.00 ± 0.75 | kJ/mol | NIST |
| ΔcH°liquid | -4658.30 ± 1.20 | kJ/mol | NIST |
| ΔcH°liquid | -4650.98 ± 0.79 | kJ/mol | NIST |
| μ | 0.30 | debye | KDB |
| LFL | 1.00 | % in Air | KDB |
| Tflash,oc | 269.26 | K | KDB |
| ΔfG° | 95.88 | kJ/mol | KDB |
| Δc,grossH | 4658.34 | kJ/mol | KDB |
| Δc,netH | 4350.272 | kJ/mol | KDB |
| ΔfH°gas | [-63.70; -62.30] | kJ/mol |
|
| ΔfH°gas | -62.34 | kJ/mol | KDB |
| ΔfH°gas | -63.00 | kJ/mol | NIST |
| ΔfH°gas | -63.70 | kJ/mol | NIST |
| ΔfH°gas | -62.30 | kJ/mol | NIST |
| ΔfH°liquid | [-98.37; -97.00] | kJ/mol |
|
| ΔfH°liquid | -97.70 ± 0.63 | kJ/mol | NIST |
| ΔfH°liquid | -98.37 ± 0.88 | kJ/mol | NIST |
| ΔfH°liquid | -97.00 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 12.61 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.70 | kJ/mol | NIST |
| IE | [9.27; 9.44] | eV |
|
| IE | 9.34 ± 0.08 | eV | NIST |
| IE | 9.38 ± 0.05 | eV | NIST |
| IE | 9.30 ± 0.10 | eV | NIST |
| IE | 9.27 ± 0.02 | eV | NIST |
| IE | 9.44 ± 0.00 | eV | NIST |
| log10WS | [-3.73; -3.73] |
|
|
| log10WS | -3.73 | Aq. Sol... | |
| log10WS | -3.73 | Estimat... | |
| logPoct/wat | 2.753 | Crippen Calculated Property | |
| McVol | 105.190 | ml/mol | McGowan Calculated Property |
| Pc | [2920.00; 2920.00] | kPa |
|
| Pc | 2920.00 | kPa | KDB |
| Pc | 2920.00 ± 40.00 | kPa | NIST |
| ρc | 235.65 ± 3.93 | kg/m3 | NIST |
| Inp | [681.00; 700.00] |
|
|
| Inp | 688.60 | NIST | |
| Inp | 681.10 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 685.90 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 688.60 | NIST | |
| Inp | 688.70 | NIST | |
| Inp | 688.60 | NIST | |
| Inp | 688.70 | NIST | |
| Inp | 681.80 | NIST | |
| Inp | 682.30 | NIST | |
| Inp | 691.80 | NIST | |
| Inp | 691.80 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.10 | NIST | |
| Inp | 688.90 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.60 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 693.90 | NIST | |
| Inp | 693.90 | NIST | |
| Inp | 693.80 | NIST | |
| Inp | 693.80 | NIST | |
| Inp | 693.80 | NIST | |
| Inp | 693.80 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.80 | NIST | |
| Inp | 689.20 | NIST | |
| Inp | 689.60 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 690.90 | NIST | |
| Inp | 687.30 | NIST | |
| Inp | 687.70 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 688.40 | NIST | |
| Inp | 688.80 | NIST | |
| Inp | 689.20 | NIST | |
| Inp | Outlier 697.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 681.80 | NIST | |
| Inp | 682.20 | NIST | |
| Inp | 681.90 | NIST | |
| Inp | 681.50 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 684.50 | NIST | |
| Inp | 682.90 | NIST | |
| Inp | 684.90 | NIST | |
| Inp | 683.60 | NIST | |
| Inp | 684.90 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 689.40 | NIST | |
| Inp | 682.10 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 683.50 | NIST | |
| Inp | 682.80 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 688.50 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 695.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.40 | NIST | |
| Inp | 690.90 | NIST | |
| Inp | 689.30 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.40 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.01 | NIST | |
| Inp | 689.10 | NIST | |
| Inp | 689.22 | NIST | |
| Inp | 691.74 | NIST | |
| Inp | 691.87 | NIST | |
| Inp | 691.94 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | Outlier 699.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 685.00 | NIST | |
| Inp | 681.30 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 682.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 683.76 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 691.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 694.00 | NIST | |
| Inp | 693.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 686.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | 683.00 | NIST | |
| Inp | 684.00 | NIST | |
| Inp | Outlier 700.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 687.00 | NIST | |
| Inp | 690.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 692.00 | NIST | |
| Inp | 681.00 | NIST | |
| Inp | 689.00 | NIST | |
| Inp | 688.00 | NIST | |
| Inp | 683.00 | NIST | |
| I | [731.00; 751.00] |
|
|
| I | 751.00 | NIST | |
| I | 751.00 | NIST | |
| I | 747.00 | NIST | |
| I | 748.00 | NIST | |
| I | 749.00 | NIST | |
| I | Outlier 731.00 | NIST | |
| I | 747.70 | NIST | |
| I | 747.30 | NIST | |
| I | 749.00 | NIST | |
| I | 747.30 | NIST | |
| I | 747.70 | NIST | |
| I | 749.00 | NIST | |
| I | 741.00 | NIST | |
| I | 736.00 | NIST | |
| I | 740.00 | NIST | |
| I | 750.00 | NIST | |
| I | 740.00 | NIST | |
| S°liquid | [327.65; 328.90] | J/mol×K |
|
| S°liquid | 327.65 | J/mol×K | NIST |
| S°liquid | 328.90 | J/mol×K | NIST |
| Tboil | 366.79 | K | KDB |
| Tc | [537.23; 537.30] | K |
|
| Tc | 537.30 | K | KDB |
| Tc | 537.30 ± 0.40 | K | NIST |
| Tc | 537.23 ± 0.05 | K | NIST |
| Tfus | [153.40; 153.69] | K |
|
| Tfus | 153.40 | K | KDB |
| Tfus | 153.69 | K | Aq. Sol... |
| Ttriple | [153.40; 154.30] | K |
|
| Ttriple | 154.30 ± 0.05 | K | NIST |
| Ttriple | 153.89 ± 0.05 | K | NIST |
| Ttriple | 153.40 ± 0.20 | K | NIST |
| Vc | [0.409; 0.409] | m3/kmol |
|
| Vc | 0.409 | m3/kmol | KDB |
| Vc | 0.409 | m3/kmol | NIST |
| Zc | 0.2673330 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [180.50; 241.81] | J/mol×K | [356.24; 523.16] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 240 400 450 500 | ||||
| Cp,gas | 180.50 | J/mol×K | 356.24 | Joback Calculated Property |
| Cp,gas | 191.75 | J/mol×K | 384.06 | Joback Calculated Property |
| Cp,gas | 202.58 | J/mol×K | 411.88 | Joback Calculated Property |
| Cp,gas | 212.98 | J/mol×K | 439.70 | Joback Calculated Property |
| Cp,gas | 222.98 | J/mol×K | 467.52 | Joback Calculated Property |
| Cp,gas | 232.58 | J/mol×K | 495.34 | Joback Calculated Property |
| Cp,gas | 241.81 | J/mol×K | 523.16 | Joback Calculated Property |
| Cp,liquid | [211.79; 212.84] | J/mol×K | [295.10; 298.15] |
|
| Cp,liquid | 212.84 | J/mol×K | 295.10 | NIST |
| Cp,liquid | 211.79 | J/mol×K | 298.15 | NIST |
| η | [0.0002312; 0.0041197] | Pa×s | [166.89; 356.24] |
|
|
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 200 250 300 350 | ||||
| η | 0.0041197 | Pa×s | 166.89 | Joback Calculated Property |
| η | 0.0017402 | Pa×s | 198.45 | Joback Calculated Property |
| η | 0.0009312 | Pa×s | 230.01 | Joback Calculated Property |
| η | 0.0005794 | Pa×s | 261.56 | Joback Calculated Property |
| η | 0.0003993 | Pa×s | 293.12 | Joback Calculated Property |
| η | 0.0002959 | Pa×s | 324.68 | Joback Calculated Property |
| η | 0.0002312 | Pa×s | 356.24 | Joback Calculated Property |
| ΔfusH | [12.64; 12.66] | kJ/mol | [153.40; 154.30] |
|
| ΔfusH | 12.66 | kJ/mol | 153.40 | NIST |
| ΔfusH | 12.64 | kJ/mol | 154.30 | NIST |
| ΔfusH | 12.66 | kJ/mol | 154.30 | NIST |
| ΔvapH | [31.09; 35.93] | kJ/mol | [283.50; 366.80] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 36 300 320 340 360 | ||||
| ΔvapH | 35.90 | kJ/mol | 283.50 | NIST |
| ΔvapH | 35.93 | kJ/mol | 300.00 | NIST |
| ΔvapH | 35.30 | kJ/mol | 306.50 | NIST |
| ΔvapH | 34.50 | kJ/mol | 317.50 | NIST |
| ΔvapH | 34.60 | kJ/mol | 339.50 | NIST |
| ΔvapH | 33.90 | kJ/mol | 347.00 | NIST |
| ΔvapH | 31.09 | kJ/mol | 366.80 | KDB |
| n0 | [1.39713; 1.39992] | [293.15; 298.15] |
|
|
| n0 | 1.39992 | 293.15 | Excess ... | |
| n0 | 1.39713 | 298.15 | KDB | |
| ρl | 697.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | 82.54 | J/mol×K | 153.40 | NIST |
| γ | 0.02 | N/m | 298.20 | KDB |
| λ | [0.11; 0.13] | W/m×K | [262.46; 321.08] |
|
|
T(K) Liquid thermal conductivity (W/m×K) 0.12 0.12 0.13 0.13 280 300 320 | ||||
| λ | 0.13 | W/m×K | 262.46 | Thermal... |
| λ | 0.13 | W/m×K | 262.75 | Thermal... |
| λ | 0.13 | W/m×K | 262.97 | Thermal... |
| λ | 0.13 | W/m×K | 280.48 | Thermal... |
| λ | 0.13 | W/m×K | 280.80 | Thermal... |
| λ | 0.13 | W/m×K | 281.03 | Thermal... |
| λ | 0.12 | W/m×K | 297.36 | Thermal... |
| λ | 0.12 | W/m×K | 297.71 | Thermal... |
| λ | 0.12 | W/m×K | 297.95 | Thermal... |
| λ | 0.11 | W/m×K | 320.47 | Thermal... |
| λ | 0.11 | W/m×K | 320.83 | Thermal... |
| λ | 0.11 | W/m×K | 321.08 | Thermal... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.53 | 100.00 | 705.5 |
| 283.53 | 500.00 | 705.9 |
| 283.53 | 1000.00 | 706.4 |
| 283.53 | 3000.00 | 708.2 |
| 283.53 | 5000.00 | 710.0 |
| 283.53 | 10000.00 | 714.3 |
| 283.52 | 15000.00 | 718.3 |
| 283.52 | 20000.00 | 722.2 |
| 283.52 | 25000.00 | 725.9 |
| 283.52 | 30000.00 | 729.4 |
| 283.52 | 35000.00 | 732.9 |
| 283.52 | 40000.00 | 736.1 |
| 283.53 | 45000.00 | 739.3 |
| 283.53 | 50000.00 | 742.4 |
| 283.52 | 55000.00 | 745.3 |
| 283.53 | 60000.00 | 748.2 |
| 283.54 | 70000.00 | 753.8 |
| 283.53 | 80000.00 | 759.0 |
| 283.53 | 90000.00 | 763.9 |
| 283.54 | 100000.00 | 768.7 |
| 293.45 | 100.00 | 697.0 |
| 293.45 | 500.00 | 697.4 |
| 293.45 | 1000.00 | 697.9 |
| 293.46 | 3000.00 | 699.9 |
| 293.45 | 5000.00 | 701.8 |
| 293.46 | 10000.00 | 706.4 |
| 293.46 | 15000.00 | 710.7 |
| 293.45 | 20000.00 | 714.8 |
| 293.45 | 25000.00 | 718.7 |
| 293.45 | 30000.00 | 722.4 |
| 293.45 | 35000.00 | 726.0 |
| 293.46 | 40000.00 | 729.4 |
| 293.46 | 45000.00 | 732.8 |
| 293.46 | 50000.00 | 736.0 |
| 293.45 | 55000.00 | 739.0 |
| 293.45 | 60000.00 | 742.0 |
| 293.45 | 70000.00 | 747.8 |
| 293.45 | 80000.00 | 753.2 |
| 293.45 | 90000.00 | 758.3 |
| 293.45 | 100000.00 | 763.1 |
| 303.37 | 100.00 | 688.4 |
| 303.37 | 500.00 | 688.9 |
| 303.38 | 1000.00 | 689.5 |
| 303.38 | 3000.00 | 691.6 |
| 303.38 | 5000.00 | 693.6 |
| 303.38 | 10000.00 | 698.5 |
| 303.38 | 15000.00 | 703.1 |
| 303.38 | 20000.00 | 707.4 |
| 303.38 | 25000.00 | 711.5 |
| 303.38 | 30000.00 | 715.4 |
| 303.38 | 35000.00 | 719.2 |
| 303.38 | 40000.00 | 722.8 |
| 303.38 | 45000.00 | 726.2 |
| 303.38 | 50000.00 | 729.5 |
| 303.37 | 55000.00 | 732.8 |
| 303.38 | 60000.00 | 735.9 |
| 303.38 | 70000.00 | 741.8 |
| 303.38 | 80000.00 | 747.4 |
| 303.38 | 90000.00 | 752.6 |
| 303.37 | 100000.00 | 757.7 |
| 313.29 | 100.00 | 680.6 |
| 313.30 | 500.00 | 681.1 |
| 313.31 | 1000.00 | 681.8 |
| 313.31 | 3000.00 | 684.0 |
| 313.30 | 5000.00 | 686.2 |
| 313.31 | 10000.00 | 691.3 |
| 313.31 | 15000.00 | 696.3 |
| 313.30 | 20000.00 | 700.9 |
| 313.30 | 25000.00 | 705.2 |
| 313.30 | 30000.00 | 709.3 |
| 313.30 | 35000.00 | 713.3 |
| 313.30 | 40000.00 | 717.0 |
| 313.30 | 45000.00 | 720.6 |
| 313.30 | 50000.00 | 724.0 |
| 313.30 | 55000.00 | 727.4 |
| 313.30 | 60000.00 | 730.6 |
| 313.30 | 70000.00 | 736.8 |
| 313.30 | 80000.00 | 742.6 |
| 313.30 | 90000.00 | 748.0 |
| 313.30 | 100000.00 | 753.1 |
| 323.18 | 100.00 | 670.5 |
| 323.18 | 500.00 | 671.0 |
| 323.18 | 1000.00 | 671.6 |
| 323.18 | 3000.00 | 674.1 |
| 323.19 | 5000.00 | 676.4 |
| 323.18 | 10000.00 | 682.0 |
| 323.19 | 15000.00 | 687.1 |
| 323.19 | 20000.00 | 692.0 |
| 323.18 | 25000.00 | 696.6 |
| 323.18 | 30000.00 | 700.9 |
| 323.18 | 35000.00 | 705.0 |
| 323.18 | 40000.00 | 708.9 |
| 323.18 | 45000.00 | 712.7 |
| 323.18 | 50000.00 | 716.3 |
| 323.18 | 55000.00 | 719.7 |
| 323.18 | 60000.00 | 723.1 |
| 323.18 | 70000.00 | 729.6 |
| 323.18 | 80000.00 | 735.5 |
| 323.19 | 90000.00 | 741.1 |
| 323.19 | 100000.00 | 746.4 |
| 333.04 | 100.00 | 661.5 |
| 333.04 | 500.00 | 662.0 |
| 333.04 | 1000.00 | 662.7 |
| 333.05 | 3000.00 | 665.3 |
| 333.05 | 5000.00 | 667.9 |
| 333.05 | 10000.00 | 673.8 |
| 333.05 | 15000.00 | 679.3 |
| 333.05 | 20000.00 | 684.5 |
| 333.05 | 25000.00 | 689.3 |
| 333.05 | 30000.00 | 693.8 |
| 333.05 | 35000.00 | 698.1 |
| 333.05 | 40000.00 | 702.2 |
| 333.05 | 45000.00 | 706.2 |
| 333.05 | 50000.00 | 709.9 |
| 333.05 | 55000.00 | 713.5 |
| 333.05 | 60000.00 | 717.0 |
| 333.05 | 70000.00 | 723.7 |
| 333.05 | 80000.00 | 729.9 |
| 333.05 | 90000.00 | 735.7 |
| 333.05 | 100000.00 | 741.1 |
| 342.91 | 100.00 | 652.7 |
| 342.91 | 500.00 | 653.3 |
| 342.91 | 1000.00 | 654.0 |
| 342.91 | 3000.00 | 656.9 |
| 342.92 | 5000.00 | 659.6 |
| 342.92 | 10000.00 | 666.0 |
| 342.91 | 15000.00 | 671.8 |
| 342.92 | 20000.00 | 677.4 |
| 342.92 | 25000.00 | 682.4 |
| 342.91 | 30000.00 | 687.1 |
| 342.91 | 35000.00 | 691.7 |
| 342.92 | 40000.00 | 696.0 |
| 342.92 | 45000.00 | 700.1 |
| 342.92 | 50000.00 | 703.9 |
| 342.92 | 55000.00 | 707.7 |
| 342.92 | 60000.00 | 711.3 |
| 342.92 | 70000.00 | 718.3 |
| 342.92 | 80000.00 | 724.6 |
| 342.92 | 90000.00 | 730.6 |
| 342.92 | 100000.00 | 736.2 |
| 352.80 | 100.00 | 644.3 |
| 352.80 | 500.00 | 644.9 |
| 352.81 | 1000.00 | 645.7 |
| 352.81 | 3000.00 | 648.8 |
| 352.81 | 5000.00 | 651.6 |
| 352.81 | 10000.00 | 658.4 |
| 352.81 | 15000.00 | 664.7 |
| 352.81 | 20000.00 | 670.5 |
| 352.81 | 25000.00 | 675.8 |
| 352.81 | 30000.00 | 680.9 |
| 352.81 | 35000.00 | 685.6 |
| 352.80 | 40000.00 | 690.0 |
| 352.80 | 45000.00 | 694.3 |
| 352.80 | 50000.00 | 698.4 |
| 352.81 | 55000.00 | 702.3 |
| 352.81 | 60000.00 | 706.0 |
| 352.80 | 70000.00 | 713.2 |
| 352.80 | 80000.00 | 719.7 |
| 352.80 | 90000.00 | 725.9 |
| 352.80 | 100000.00 | 731.7 |
| 362.68 | 100.00 | 633.6 |
| 362.68 | 500.00 | 634.3 |
| 362.69 | 1000.00 | 635.0 |
| 362.69 | 3000.00 | 638.5 |
| 362.69 | 5000.00 | 641.7 |
| 362.70 | 10000.00 | 649.1 |
| 362.70 | 15000.00 | 655.8 |
| 362.69 | 20000.00 | 661.9 |
| 362.70 | 25000.00 | 667.6 |
| 362.69 | 30000.00 | 672.8 |
| 362.69 | 35000.00 | 677.8 |
| 362.69 | 40000.00 | 682.5 |
| 362.69 | 45000.00 | 687.0 |
| 362.69 | 50000.00 | 691.2 |
| 362.69 | 55000.00 | 695.2 |
| 362.69 | 60000.00 | 699.1 |
| 362.69 | 70000.00 | 706.6 |
| 362.69 | 80000.00 | 713.4 |
| 362.69 | 90000.00 | 719.7 |
| 362.68 | 100000.00 | 725.7 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 98.00 | 298.15 | 694.51 |
| 98.00 | 303.15 | 689.57 |
| 98.00 | 312.83 | 680.92 |
| 98.00 | 322.39 | 672.17 |
| 98.00 | 327.49 | 668.07 |
| 98.00 | 340.21 | 655.95 |
| 98.00 | 354.73 | 643.5 |
| 98.00 | 360.03 | 638.93 |
| 24510.00 | 298.15 | 718.23 |
| 24510.00 | 303.15 | 715.0 |
| 24510.00 | 327.47 | 697.97 |
| 24510.00 | 360.06 | 672.86 |
| 24510.00 | 392.79 | 646.48 |
| 24510.00 | 424.11 | 619.97 |
| 24510.00 | 452.35 | 595.84 |
| 24510.00 | 473.70 | 578.48 |
| 49030.00 | 298.15 | 734.7 |
| 49030.00 | 303.15 | 733.1 |
| 49030.00 | 327.49 | 718.4 |
| 49030.00 | 359.96 | 699.31 |
| 49030.00 | 392.68 | 676.29 |
| 49030.00 | 424.17 | 653.79 |
| 49030.00 | 452.34 | 628.89 |
| 49030.00 | 473.56 | 612.5 |
| 98060.00 | 298.15 | 765.58 |
| 98060.00 | 303.15 | 761.82 |
| 98060.00 | 327.48 | 746.71 |
| 98060.00 | 359.87 | 730.37 |
| 98060.00 | 392.74 | 714.89 |
| 98060.00 | 424.17 | 697.03 |
| 98060.00 | 452.25 | 676.86 |
| 98060.00 | 473.47 | 665.45 |
| 147100.00 | 298.15 | 783.57 |
| 147100.00 | 303.15 | 780.46 |
| 147100.00 | 327.63 | 767.87 |
| 147100.00 | 359.74 | 750.76 |
| 147100.00 | 392.61 | 734.09 |
| 147100.00 | 424.04 | 717.45 |
| 147100.00 | 452.28 | 702.95 |
| 147100.00 | 473.33 | 692.3 |
| 196130.00 | 298.15 | 800.85 |
| 196130.00 | 303.15 | 797.46 |
| 196130.00 | 327.63 | 786.42 |
| 196130.00 | 359.75 | 773.85 |
| 196130.00 | 392.46 | 758.9 |
| 196130.00 | 423.82 | 745.35 |
| 196130.00 | 452.22 | 733.49 |
| 196130.00 | 473.28 | 723.12 |
| 245160.00 | 298.15 | 816.79 |
| 245160.00 | 303.15 | 815.3 |
| 245160.00 | 327.67 | 805.58 |
| 245160.00 | 359.63 | 791.61 |
| 245160.00 | 392.40 | 776.73 |
| 245160.00 | 424.07 | 760.78 |
| 245160.00 | 452.27 | 750.38 |
| 245160.00 | 473.35 | 737.15 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [266.18; 391.88] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43101e+01 | |||
| Coefficient B | -3.15735e+03 | |||
| Coefficient C | -4.10140e+01 | |||
| Temperature range, min. | 266.18 | |||
| Temperature range, max. | 391.88 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
| Pvap | 1.33 | kPa | 266.18 | Calculated Property |
| Pvap | 3.02 | kPa | 280.15 | Calculated Property |
| Pvap | 6.27 | kPa | 294.11 | Calculated Property |
| Pvap | 12.03 | kPa | 308.08 | Calculated Property |
| Pvap | 21.66 | kPa | 322.05 | Calculated Property |
| Pvap | 36.86 | kPa | 336.01 | Calculated Property |
| Pvap | 59.80 | kPa | 349.98 | Calculated Property |
| Pvap | 93.04 | kPa | 363.95 | Calculated Property |
| Pvap | 139.54 | kPa | 377.91 | Calculated Property |
| Pvap | 202.63 | kPa | 391.88 | Calculated Property |
| Pvap | [1.28e-06; 2846.43] | kPa | [154.27; 537.29] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.49146e+01 | |||
| Coefficient B | -7.03286e+03 | |||
| Coefficient C | -1.05363e+01 | |||
| Coefficient D | 8.19459e-06 | |||
| Temperature range, min. | 154.27 | |||
| Temperature range, max. | 537.29 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
| Pvap | 1.28e-06 | kPa | 154.27 | Calculated Property |
| Pvap | 2.12e-03 | kPa | 196.83 | Calculated Property |
| Pvap | 0.18 | kPa | 239.39 | Calculated Property |
| Pvap | 3.25 | kPa | 281.94 | Calculated Property |
| Pvap | 24.06 | kPa | 324.50 | Calculated Property |
| Pvap | 103.16 | kPa | 367.06 | Calculated Property |
| Pvap | 311.67 | kPa | 409.62 | Calculated Property |
| Pvap | 747.67 | kPa | 452.17 | Calculated Property |
| Pvap | 1536.71 | kPa | 494.73 | Calculated Property |
| Pvap | 2846.43 | kPa | 537.29 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Heptene.
Mixtures
- 1-Heptene + Ethanol, 2,2'-oxybis-
- 1-Heptene + Triethylene glycol
- 1,2-Ethanediol + 1-Heptene
- Acetic acid, pentyl ester + 1-Heptene
- 1-Propanol + 1-Heptene
- 1-Heptene + Pyridine
- 1,2-Ethanediol + 1-Heptene + Tetramethylammonium chloride
- 1-Heptene + Tetramethylammonium chloride + Glycerin
- 2-Furanmethanol + 1-Heptene
- 1-Heptene + N-Formylmorpholine
- 1-Heptene + 2-Pyrrolidinone, 1-methyl-
- 1-Heptene + Propanamide, N,N-bis(2-ethylhexyl)-2-methyl-
- 1-Heptene + 1-Octadecanol
- 1-Heptene + 1-Eicosanol
- 1-Heptene + 1,8-Diaminooctane
- 1-Heptene + 1,10-Diaminodecane
- 1-Heptene + 1,12-Dodecanediamine
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, trihexyl(tetradecyl)-phosphonium tris(pentafluoroethyl) trifluorophosphate, by gas liquid chromatography
- Determination of activity coefficients at infinite dilution of organic solutes in the ionic liquid, tributylmethylphosphonium methylsulphate by gas liquid chromatography
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- 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
- Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
- 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
- Measurements of different thermodynamic properties of systems containing ionic liquids and correlation of these properties using modified UNIFAC (Dortmund)
- 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
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Activity coefficients at infinite dilution for hydrocarbons in furfuryl alcohol at T=(278.15 and 298.15) K, determined by g.l.c.
- 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
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- 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
- 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
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- 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.
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Activity coefficients at infinite dilution 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
- 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 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
- 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 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
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- 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
- 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
- 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
- Use of water in aiding olefin/paraffin (liquid + liquid) extraction via complexation with a silver bis(trifluoromethylsulfonyl)imide salt
- 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
- Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- 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
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- 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 Density of n-Pentene, n-Hexene, and n-Heptene at Temperatures from 283.15 to 363.15 K and Pressures up to 100 MPa
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Hexyl-3-methylimidazolium Hexafluorophosphate from Gas-Liquid Chromatography
- 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
- Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
- 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
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- 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
- 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
- Infinite Dilution Activity Coefficients for Trihexyltetradecyl Phosphonium Ionic Liquids: Measurements and COSMO-RS Prediction
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Excess Volume of the 1-Propanol + 1-Alkene Systems in Terms of an Equation of State with Association
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Experimental Study and Correlation Models of the Density and Viscosity of 1-Hexene and 1-Heptene at Temperatures from (298 to 473) K and Pressures up to 245 MPa
- Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
- 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
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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