- InChI
- InChI=1S/C8H16/c1-3-5-7-8-6-4-2/h3H,1,4-8H2,2H3
- InChI Key
- KWKAKUADMBZCLK-UHFFFAOYSA-N
- Formula
- C8H16
- SMILES
- C=CCCCCCC
- Molecular Weight1
- 112.21
- CAS
- 111-66-0
- Other Names
-
- 1-C8H16
- 1-n-Octene
- CAPRYLENE
- N-1-OCTENE
- NSC 8457
- Neodene 8
- Oct-1-ene
- Octene-1
- Octylene
- SHOP C8
- «alpha»-Octene
- «alpha»-Octylene
- «alpha»-Octene
- «alpha»-Octylene
- 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,cc : Flash Point (Closed 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- D*i : Self diffusion coefficient (m2/s).
- 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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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3860 | KDB | |
| Tig | 529.26 | K | KDB |
| AP | 305.650 | K | KDB |
| ΔcH°liquid | -5312.90 ± 1.10 | kJ/mol | NIST |
| μ | 0.30 | debye | KDB |
| LFL | 0.90 | % in Air | KDB |
| Tflash,cc | 294.26 | K | KDB |
| ΔfG° | 104.30 | kJ/mol | KDB |
| Δc,grossH | 5312.93 | kJ/mol | KDB |
| Δc,netH | 4960.844 | kJ/mol | KDB |
| ΔfH°gas | [-82.98; -82.93] | kJ/mol |
|
| ΔfH°gas | -82.98 | kJ/mol | KDB |
| ΔfH°gas | -82.93 | kJ/mol | NIST |
| ΔfH°gas | -82.93 | kJ/mol | NIST |
| ΔfH°liquid | -121.80 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 15.20 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [38.00; 40.60] | kJ/mol |
|
| ΔvapH° | 40.44 | kJ/mol | NIST |
| ΔvapH° | 40.60 | kJ/mol | NIST |
| ΔvapH° | 40.27 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 40.30 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 38.00 | kJ/mol | NIST |
| IE | [9.43; 9.60] | eV |
|
| IE | 9.43 ± 0.01 | eV | NIST |
| IE | 9.43 ± 0.01 | eV | NIST |
| IE | 9.43 ± 0.01 | eV | NIST |
| IE | 9.60 ± 0.01 | eV | NIST |
| log10WS | [-4.44; -4.44] |
|
|
| log10WS | -4.44 | Aq. Sol... | |
| log10WS | -4.44 | Estimat... | |
| logPoct/wat | 3.143 | Crippen Calculated Property | |
| McVol | 119.280 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [2680.00; 2680.00] | kPa |
|
| Pc | 2680.00 | kPa | KDB |
| Pc | 2680.00 ± 80.00 | kPa | NIST |
| ρc | 235.65 ± 8.98 | kg/m3 | NIST |
| Inp | [779.00; 799.00] |
|
|
| Inp | 786.00 | NIST | |
| Inp | 788.30 | NIST | |
| Inp | 780.40 | NIST | |
| Inp | 784.90 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 780.00 | NIST | |
| Inp | 785.30 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.30 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 781.80 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 792.50 | NIST | |
| Inp | 792.60 | NIST | |
| Inp | 792.70 | NIST | |
| Inp | 792.80 | NIST | |
| Inp | 792.90 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.40 | NIST | |
| Inp | 788.60 | NIST | |
| Inp | 788.80 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 786.70 | NIST | |
| Inp | 789.40 | NIST | |
| Inp | 788.10 | NIST | |
| Inp | 787.70 | NIST | |
| Inp | 787.60 | NIST | |
| Inp | 787.30 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 786.60 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 781.60 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 782.60 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 783.70 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 782.67 | NIST | |
| Inp | 782.67 | NIST | |
| Inp | 782.70 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 789.20 | NIST | |
| Inp | 781.40 | NIST | |
| Inp | 781.00 | NIST | |
| Inp | 782.90 | NIST | |
| Inp | 782.30 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | Outlier 779.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | Outlier 796.00 | NIST | |
| Inp | 787.72 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 792.90 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 782.40 | NIST | |
| Inp | 789.30 | NIST | |
| Inp | 788.40 | NIST | |
| Inp | 788.30 | NIST | |
| Inp | 789.30 | NIST | |
| Inp | 789.10 | NIST | |
| Inp | 789.60 | NIST | |
| Inp | 788.40 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 789.70 | NIST | |
| Inp | 788.30 | NIST | |
| Inp | 789.30 | NIST | |
| Inp | 789.10 | NIST | |
| Inp | 789.30 | NIST | |
| Inp | 788.40 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 789.04 | NIST | |
| Inp | 788.99 | NIST | |
| Inp | 789.05 | NIST | |
| Inp | 791.72 | NIST | |
| Inp | 791.76 | NIST | |
| Inp | 791.77 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | Outlier 799.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 782.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | Outlier 796.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | Outlier 799.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | Outlier 799.00 | NIST | |
| Inp | 788.20 | NIST | |
| Inp | 788.04 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | Outlier 779.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 793.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | 792.00 | NIST | |
| Inp | Outlier 797.00 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 784.90 | NIST | |
| Inp | 783.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 785.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 782.00 | NIST | |
| I | [822.00; 892.00] |
|
|
| I | 851.00 | NIST | |
| I | 852.00 | NIST | |
| I | 847.00 | NIST | |
| I | 847.00 | NIST | |
| I | 850.00 | NIST | |
| I | 848.50 | NIST | |
| I | 847.40 | NIST | |
| I | 847.20 | NIST | |
| I | 849.90 | NIST | |
| I | 847.20 | NIST | |
| I | 848.50 | NIST | |
| I | 847.40 | NIST | |
| I | 849.90 | NIST | |
| I | 842.00 | NIST | |
| I | 837.00 | NIST | |
| I | 833.00 | NIST | |
| I | 836.00 | NIST | |
| I | 837.00 | NIST | |
| I | Outlier 892.00 | NIST | |
| I | 850.00 | NIST | |
| I | 822.00 | NIST | |
| I | 830.00 | NIST | |
| I | 830.00 | NIST | |
| I | 831.00 | NIST | |
| I | 830.00 | NIST | |
| I | 836.00 | NIST | |
| S°liquid | 360.45 | J/mol×K | NIST |
| Tboil | 394.44 | K | KDB |
| Tc | [566.55; 567.00] | K |
|
| Tc | 567.00 | K | KDB |
| Tc | 567.00 ± 0.80 | K | NIST |
| Tc | 566.60 | K | NIST |
| Tc | 566.55 ± 0.05 | K | NIST |
| Tfus | [167.15; 171.44] | K |
|
| Tfus | 171.40 | K | KDB |
| Tfus | 171.25 | K | Aq. Sol... |
| Tfus | 171.31 ± 0.20 | K | NIST |
| Tfus | 171.43 ± 0.05 | K | NIST |
| Tfus | 171.44 ± 0.03 | K | NIST |
| Tfus | 171.20 ± 1.00 | K | NIST |
| Tfus | 171.44 ± 0.03 | K | NIST |
| Tfus | 171.40 ± 0.06 | K | NIST |
| Tfus | 171.09 ± 0.10 | K | NIST |
| Tfus | 171.05 ± 0.40 | K | NIST |
| Tfus | Outlier 167.15 ± 1.50 | K | NIST |
| Tfus | 171.04 ± 0.30 | K | NIST |
| Ttriple | 171.46 ± 0.05 | K | NIST |
| Vc | [0.468; 0.468] | m3/kmol |
|
| Vc | 0.468 | m3/kmol | KDB |
| Vc | 0.468 | m3/kmol | NIST |
| Zc | 0.2660490 | KDB | |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [217.72; 285.74] | J/mol×K | [379.12; 545.88] |
|
| Cp,gas | 217.72 | J/mol×K | 379.12 | Joback Calculated Property |
| Cp,gas | 230.22 | J/mol×K | 406.91 | Joback Calculated Property |
| Cp,gas | 242.23 | J/mol×K | 434.71 | Joback Calculated Property |
| Cp,gas | 253.77 | J/mol×K | 462.50 | Joback Calculated Property |
| Cp,gas | 264.86 | J/mol×K | 490.29 | Joback Calculated Property |
| Cp,gas | 275.52 | J/mol×K | 518.08 | Joback Calculated Property |
| Cp,gas | 285.74 | J/mol×K | 545.88 | Joback Calculated Property |
| Cp,liquid | 241.21 | J/mol×K | 298.15 | NIST |
| η | [0.0002381; 0.0046461] | Pa×s | [178.16; 379.12] |
|
| η | 0.0046461 | Pa×s | 178.16 | Joback Calculated Property |
| η | 0.0019138 | Pa×s | 211.65 | Joback Calculated Property |
| η | 0.0010045 | Pa×s | 245.15 | Joback Calculated Property |
| η | 0.0006156 | Pa×s | 278.64 | Joback Calculated Property |
| η | 0.0004191 | Pa×s | 312.13 | Joback Calculated Property |
| η | 0.0003074 | Pa×s | 345.63 | Joback Calculated Property |
| η | 0.0002381 | Pa×s | 379.12 | Joback Calculated Property |
| ΔfusH | [15.31; 15.31] | kJ/mol | [171.46; 171.50] |
|
| ΔfusH | 15.31 | kJ/mol | 171.46 | NIST |
| ΔfusH | 15.31 | kJ/mol | 171.50 | NIST |
| ΔfusH | 15.31 | kJ/mol | 171.50 | NIST |
| ΔvapH | [33.77; 41.20] | kJ/mol | [275.50; 395.20] |
|
| ΔvapH | 41.20 | kJ/mol | 275.50 | NIST |
| ΔvapH | 40.20 | kJ/mol | 277.00 | NIST |
| ΔvapH | 39.50 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 38.60 ± 0.10 | kJ/mol | 328.00 | NIST |
| ΔvapH | 37.60 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 38.80 | kJ/mol | 356.00 | NIST |
| ΔvapH | 36.60 ± 0.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 35.80 ± 0.10 | kJ/mol | 368.00 | NIST |
| ΔvapH | 34.07 | kJ/mol | 394.40 | NIST |
| ΔvapH | 33.77 | kJ/mol | 395.20 | KDB |
| Pvap | [8.30; 165.90] | kPa | [323.15; 413.15] |
|
| Pvap | 8.30 | kPa | 323.15 | Isother... |
| Pvap | 10.12 | kPa | 328.15 | Vapor L... |
| Pvap | 38.51 | kPa | 363.15 | Measure... |
| Pvap | 39.20 | kPa | 363.15 | Vapor L... |
| Pvap | 53.82 | kPa | 373.10 | Phase E... |
| Pvap | 165.90 | kPa | 413.15 | Phase E... |
| n0 | 1.40620 | 298.15 | KDB | |
| ρl | [710.88; 715.00] | kg/m3 | [293.00; 298.15] |
|
| ρl | 715.00 | kg/m3 | 293.00 | KDB |
| ρl | 710.88 | kg/m3 | 298.15 | Excess ... |
| D*i | [2.28e-07; 3.44e-07] | m2/s | [298.15; 323.15] |
|
| D*i | 2.28e-07 | m2/s | 298.15 | Viscosi... |
| D*i | 3.44e-07 | m2/s | 323.15 | Viscosi... |
| ΔfusS | 89.31 | J/mol×K | 171.46 | NIST |
| γ | [0.02; 0.02] | N/m | [283.10; 348.15] |
|
| γ | 0.02 | N/m | 283.10 | Phase E... |
| γ | 0.02 | N/m | 298.15 | Phase E... |
| γ | 0.02 | N/m | 298.20 | KDB |
| γ | 0.02 | N/m | 323.15 | Phase E... |
| γ | 0.02 | N/m | 348.15 | Phase E... |
| λ | [0.12; 0.14] | W/m×K | [259.69; 326.87] |
|
| λ | 0.14 | W/m×K | 259.69 | Thermal... |
| λ | 0.14 | W/m×K | 259.90 | Thermal... |
| λ | 0.14 | W/m×K | 260.06 | Thermal... |
| λ | 0.13 | W/m×K | 279.34 | Thermal... |
| λ | 0.13 | W/m×K | 279.57 | Thermal... |
| λ | 0.13 | W/m×K | 279.72 | Thermal... |
| λ | 0.12 | W/m×K | 296.88 | Thermal... |
| λ | 0.12 | W/m×K | 297.14 | Thermal... |
| λ | 0.12 | W/m×K | 297.28 | Thermal... |
| λ | 0.12 | W/m×K | 315.82 | Thermal... |
| λ | 0.12 | W/m×K | 316.07 | Thermal... |
| λ | 0.12 | W/m×K | 316.24 | Thermal... |
| λ | 0.12 | W/m×K | 326.44 | Thermal... |
| λ | 0.12 | W/m×K | 326.70 | Thermal... |
| λ | 0.12 | W/m×K | 326.87 | Thermal... |
Datasets
Thermal conductivity, W/m/K
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Thermal conductivity, W/m/K - Liquid |
| 254.47 | 100.00 | 0.1381 |
| 254.41 | 5000.00 | 0.1402 |
| 254.47 | 10000.00 | 0.1426 |
| 254.35 | 20000.00 | 0.1464 |
| 254.35 | 30000.00 | 0.1500 |
| 274.46 | 100.00 | 0.1302 |
| 274.44 | 5000.00 | 0.1324 |
| 274.50 | 10000.00 | 0.1349 |
| 274.59 | 20000.00 | 0.1394 |
| 274.44 | 30000.00 | 0.1439 |
| 294.91 | 100.00 | 0.1254 |
| 294.90 | 5200.00 | 0.1277 |
| 294.85 | 10100.00 | 0.1300 |
| 294.79 | 20000.00 | 0.1341 |
| 294.76 | 30000.00 | 0.1379 |
| 314.65 | 100.00 | 0.1200 |
| 314.61 | 5000.00 | 0.1228 |
| 314.59 | 10000.00 | 0.1249 |
| 314.61 | 20000.00 | 0.1291 |
| 314.51 | 30000.00 | 0.1331 |
| 334.94 | 100.00 | 0.1140 |
| 334.82 | 5100.00 | 0.1167 |
| 334.82 | 10000.00 | 0.1191 |
| 334.69 | 20000.00 | 0.1238 |
| 334.71 | 30000.00 | 0.1282 |
| 355.05 | 100.00 | 0.1078 |
| 354.89 | 5100.00 | 0.1106 |
| 354.72 | 10000.00 | 0.1137 |
| 354.74 | 20000.00 | 0.1186 |
| 354.64 | 30000.00 | 0.1234 |
| 374.48 | 600.00 | 0.1023 |
| 375.03 | 5100.00 | 0.1047 |
| 374.83 | 10000.00 | 0.1077 |
| 374.86 | 20100.00 | 0.1135 |
| 374.80 | 30000.00 | 0.1179 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [287.65; 421.80] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.42819e+01 | |||
| Coefficient B | -3.35220e+03 | |||
| Coefficient C | -4.81090e+01 | |||
| Temperature range, min. | 287.65 | |||
| Temperature range, max. | 421.80 | |||
| Pvap | 1.33 | kPa | 287.65 | Calculated Property |
| Pvap | 3.03 | kPa | 302.56 | Calculated Property |
| Pvap | 6.27 | kPa | 317.46 | Calculated Property |
| Pvap | 12.05 | kPa | 332.37 | Calculated Property |
| Pvap | 21.69 | kPa | 347.27 | Calculated Property |
| Pvap | 36.91 | kPa | 362.18 | Calculated Property |
| Pvap | 59.86 | kPa | 377.08 | Calculated Property |
| Pvap | 93.10 | kPa | 391.99 | Calculated Property |
| Pvap | 139.59 | kPa | 406.89 | Calculated Property |
| Pvap | 202.63 | kPa | 421.80 | Calculated Property |
| Pvap | [2.43e-06; 2579.57] | kPa | [171.45; 566.60] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 9.67823e+01 | |||
| Coefficient B | -8.07486e+03 | |||
| Coefficient C | -1.22214e+01 | |||
| Coefficient D | 8.73474e-06 | |||
| Temperature range, min. | 171.45 | |||
| Temperature range, max. | 566.60 | |||
| Pvap | 2.43e-06 | kPa | 171.45 | Calculated Property |
| Pvap | 2.57e-03 | kPa | 215.36 | Calculated Property |
| Pvap | 0.18 | kPa | 259.26 | Calculated Property |
| Pvap | 3.04 | kPa | 303.17 | Calculated Property |
| Pvap | 21.74 | kPa | 347.07 | Calculated Property |
| Pvap | 91.75 | kPa | 390.98 | Calculated Property |
| Pvap | 275.95 | kPa | 434.88 | Calculated Property |
| Pvap | 663.70 | kPa | 478.79 | Calculated Property |
| Pvap | 1375.08 | kPa | 522.69 | Calculated Property |
| Pvap | 2579.57 | kPa | 566.60 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Octene.
Mixtures
- 1-Propanol + 1-Octene
- 1-Octene + 1-Butanol
- 1-Octene + 1-Hexanol
- 1-Octene + 1-Octanol
- 1-Octene + 1-Decanol
- 1-Octene + Ethanol, 2,2'-oxybis-
- 1-Octene + Triethylene glycol
- 1-Octene + 1,2-Ethanediol
- 1-Octene + N,N-Dimethylacetamide
- 1-Octene + Thiophene, 2-methyl-
- 1-Octene + Dimethyl ether
- 1-Octene + Octane
- 1-Octene + N-Formylmorpholine
- 1-Octene + 2-Pyrrolidinone, 1-methyl-
- 1-Hexene + 1-Octene
- 1-Octene + Propanamide, N,N-bis(2-ethylhexyl)-2-methyl-
- 1-Octene + 1,8-Diaminooctane
- 1-Octene + 1,10-Diaminodecane
- 1-Octene + 1,12-Dodecanediamine
- Carbon monoxide + 1-Octene
Find more mixtures with 1-Octene.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- 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
- Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
- Excess molar enthalpy of 1-alkanol + 1-octene mixtures at 298.15K Experimental results and theoretical description by means of the ERAS and TB models
- Experimental and predicted phase equilibria and excess properties for systems with ionic liquids
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid N-butyl-4-methylpyridinium tosylate using GLC at T = (328.15, 333.15, 338.15, and 343.15)K
- 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)
- Temperature dependence of the excess molar volume of 1-hexanol + 1-alkene systems in terms of an association and equation of state model
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- 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]
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid 1-butyl-3-methyl-imidazolium 2-(2-methoxyethoxy) ethyl sulfate using g.l.c. at T = (298.15, 303.15, and 308.15) K
- Activity coefficients at infinite dilution measurements for organic solutes in the ionic liquid hexyl-3-methyl-imidazolium bis(trifluoromethylsulfonyl)-imide using g.l.c. at T = (298.15, 313.15, and 333.15) K
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Measurement of activity coefficients at infinite dilution using polar and non-polar solutes in the ionic liquid 1-methyl-3-octyl-imidazolium diethyleneglycolmonomethylethersulfate at T = (288.15, 298.15, and 313.15) K
- 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 in the ionic liquid trihexyltetradecylphosphonium-bis-(2,4,4-trimethylpentyl)- phosphinate using g.l.c. at T = (303.15, 308.15, 313.15, and 318.15) K
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- 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
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
- 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 of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
- 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
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution 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
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution 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
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- 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
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Measurements of the density and viscosity of 1-hexene + 1-octene mixtures at high temperatures and high pressures
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- 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
- 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
- Determination of Activity Coefficients at Infinite Dilution of Solutes in the Ionic Liquid 1-Butyl-3-methylimidazolium Octyl Sulfate Using Gas-Liquid Chromatography at a Temperature of 298.15 K, 313.15 K, or 328.15 K
- 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
- 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
- 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
- Viscosity and Diffusivity for the Ionic Liquid 1-Hexyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)amide with 1-Octene
- 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
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Chemical Equilibrium of the Liquid-Phase Dehydration of 1-Octanol to 1-(Octyloxy)octane
- Enhancing liquid-phase olefin-paraffin separations using novel silver-based ionic liquids
- Isothermal Phase Equilibria and Excess Molar Enthalpies for Binary Systems with Dimethyl Ether at 323.15 K
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- 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
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Solubilities of CO and H2 in Neat and CO2-Expanded Hydroformylation Reaction Mixtures Containing 1-Octene and Nonanal up to 353.15 K and 9 MPa
- Phase Equilibrium, Volumetric, and Interfacial Properties of the Ionic Liquid, 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)amide and 1-Octene
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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