- InChI
- InChI=1S/C18H36/c1-3-5-7-9-11-13-15-17-18-16-14-12-10-8-6-4-2/h3H,1,4-18H2,2H3
- InChI Key
- CCCMONHAUSKTEQ-UHFFFAOYSA-N
- Formula
- C18H36
- SMILES
- C=CCCCCCCCCCCCCCCCC
- Molecular Weight1
- 252.48
- CAS
- 112-88-9
- Other Names
-
- Neodene 18
- Octadec-1-ene
- Octadeca-1-ene
- Octadecene-1
- Octadecylene, «alpha»-
- «alpha»-Octadecene
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.8066; 0.8370] |
|
|
| ω | 0.8370 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.8066 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.8066 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.8070 | KDB | |
| μ | 0.37 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | [186.18; 188.40] | kJ/mol |
|
| ΔfG° | 186.18 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 188.40 | kJ/mol | KDB |
| ΔfH°gas | [-289.99; -289.20] | kJ/mol |
|
| ΔfH°gas | -289.99 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -289.20 | kJ/mol | KDB |
| ΔfusH° | 41.10 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 90.00 | kJ/mol | NIST |
| IE | 9.56 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.77 | Relay (1.0) Calculated Property | |
| logPoct/wat | 7.044 | Crippen Calculated Property | |
| McVol | 260.180 | ml/mol | McGowan Calculated Property |
| Pc | [1130.00; 1144.53] | kPa |
|
| Pc | 1134.84 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 1144.53 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 1140.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 1130.00 | kPa | KDB |
| Ptriple | 9.05e-06 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1779.00; 1805.00] |
|
|
| Inp | 1793.00 | NIST | |
| Inp | 1799.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1786.80 | NIST | |
| Inp | 1787.80 | NIST | |
| Inp | 1790.00 | NIST | |
| Inp | 1795.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1786.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1792.60 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1793.50 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1788.00 | NIST | |
| Inp | 1792.60 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1793.50 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1788.00 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | 1793.10 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1788.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | 1788.00 | NIST | |
| Inp | 1790.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | Outlier 1800.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | 1788.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | Outlier 1805.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1790.00 | NIST | |
| Inp | Outlier 1779.00 | NIST | |
| Inp | 1795.00 | NIST | |
| Inp | 1793.00 | NIST | |
| Inp | 1795.00 | NIST | |
| Inp | 1792.10 | NIST | |
| Inp | 1793.50 | NIST | |
| Ip | [1823.00; 1862.00] |
|
|
| Ip | 1862.00 | NIST | |
| Ip | 1856.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | 1848.00 | NIST | |
| Ip | 1823.00 | NIST | |
| Ip | 1862.00 | NIST | |
| Tboil | [587.97; 588.00] | K |
|
| Tboil | 587.97 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 588.00 | K | KDB |
| Tc | [739.00; 739.26] | K |
|
| Tc | 739.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 739.26 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 739.26 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 739.00 | K | KDB |
| Tfus | [290.65; 291.00] | K |
|
| Tfus | 290.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 290.76 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 290.80 | K | KDB |
| Tfus | 291.00 ± 3.00 | K | NIST |
| Ttriple | 290.76 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 10.12 | ChemSep v8.3 pure component data Compiled value | |
| URi | 12.36 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [1.012; 1.153] | m3/kmol |
|
| Vc | 1.012 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 1.153 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2480000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [54.27; 76.40] | kJ/mol | [494.00; 588.00] |
|
| ΔvapH | 76.40 | kJ/mol | 494.00 | NIST |
| ΔvapH | 54.27 | kJ/mol | 588.00 | KDB |
| ρl | 789.00 | kg/m3 | 293.00 | KDB |
| γ | 0.03 | N/m | 298.20 | KDB |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [452.00; 452.20] | K | [2.00; 2.00] |
|
| Tboilr | 452.00 | K | 2.00 | NIST |
| Tboilr | 452.20 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [247.57; 1049.39] | J/mol×K | [100.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.44720e+02 | |||
| Coefficient B | -6.12286e+02 | |||
| Coefficient C | 7.17665e+00 | |||
| Coefficient D | -7.10737e-05 | |||
| Coefficient E | 1.27032e-08 | |||
| Temperature range, min. | 100.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 247.57 | J/mol×K | 100.00 | Calculated Property |
| Cp,gas | 361.87 | J/mol×K | 255.56 | Calculated Property |
| Cp,gas | 531.94 | J/mol×K | 411.11 | Calculated Property |
| Cp,gas | 673.08 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 780.74 | J/mol×K | 722.22 | Calculated Property |
| Cp,gas | 862.74 | J/mol×K | 877.78 | Calculated Property |
| Cp,gas | 926.18 | J/mol×K | 1033.33 | Calculated Property |
| Cp,gas | 976.22 | J/mol×K | 1188.89 | Calculated Property |
| Cp,gas | 1016.46 | J/mol×K | 1344.44 | Calculated Property |
| Cp,gas | 1049.39 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [539.46; 798.50] | J/mol×K | [290.76; 587.97] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 2.86040e+02 | |||
| Coefficient B | 8.71570e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 587.97 | |||
| Cp,liquid | 539.46 | J/mol×K | 290.76 | Calculated Property |
| Cp,liquid | 568.24 | J/mol×K | 323.78 | Calculated Property |
| Cp,liquid | 597.02 | J/mol×K | 356.81 | Calculated Property |
| Cp,liquid | 625.80 | J/mol×K | 389.83 | Calculated Property |
| Cp,liquid | 654.59 | J/mol×K | 422.85 | Calculated Property |
| Cp,liquid | 683.37 | J/mol×K | 455.88 | Calculated Property |
| Cp,liquid | 712.15 | J/mol×K | 488.90 | Calculated Property |
| Cp,liquid | 740.93 | J/mol×K | 521.92 | Calculated Property |
| Cp,liquid | 769.71 | J/mol×K | 554.95 | Calculated Property |
| Cp,liquid | 798.50 | J/mol×K | 587.97 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0044691; 0.0001584] | Pa×s | [290.76; 598.40] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.19070e+01 | |||
| Coefficient B | 1.88890e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 598.40 | |||
| η | 0.0044691 | Pa×s | 290.76 | Calculated Property |
| η | 0.0022564 | Pa×s | 324.94 | Calculated Property |
| η | 0.0012976 | Pa×s | 359.12 | Calculated Property |
| η | 0.0008215 | Pa×s | 393.31 | Calculated Property |
| η | 0.0005595 | Pa×s | 427.49 | Calculated Property |
| η | 0.0004034 | Pa×s | 461.67 | Calculated Property |
| η | 0.0003043 | Pa×s | 495.85 | Calculated Property |
| η | 0.0002380 | Pa×s | 530.04 | Calculated Property |
| η | 0.0001918 | Pa×s | 564.22 | Calculated Property |
| η | 0.0001584 | Pa×s | 598.40 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [85.10; 0.00] | kJ/mol | [290.76; 739.26] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 1.06070e+02 | |||
| Coefficient B | 4.40840e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 1.00000e-07 | |||
| Critical temperature, Tc (K) | 7.39260e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 748 K. | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 739.26 | |||
| ΔvapH | 85.10 | kJ/mol | 290.76 | Calculated Property |
| ΔvapH | 80.79 | kJ/mol | 340.59 | Calculated Property |
| ΔvapH | 76.17 | kJ/mol | 390.43 | Calculated Property |
| ΔvapH | 71.17 | kJ/mol | 440.26 | Calculated Property |
| ΔvapH | 65.67 | kJ/mol | 490.09 | Calculated Property |
| ΔvapH | 59.52 | kJ/mol | 539.93 | Calculated Property |
| ΔvapH | 52.43 | kJ/mol | 589.76 | Calculated Property |
| ΔvapH | 43.85 | kJ/mol | 639.59 | Calculated Property |
| ΔvapH | 32.30 | kJ/mol | 689.43 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 739.26 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [447.22; 610.23] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.55323e+01 | |||
| Coefficient B | -5.05557e+03 | |||
| Coefficient C | -1.15594e+02 | |||
| Temperature range, min. | 447.22 | |||
| Temperature range, max. | 610.23 | |||
| Pvap | 1.33 | kPa | 447.22 | Calculated Property |
| Pvap | 2.94 | kPa | 465.33 | Calculated Property |
| Pvap | 5.98 | kPa | 483.44 | Calculated Property |
| Pvap | 11.40 | kPa | 501.56 | Calculated Property |
| Pvap | 20.51 | kPa | 519.67 | Calculated Property |
| Pvap | 35.08 | kPa | 537.78 | Calculated Property |
| Pvap | 57.41 | kPa | 555.89 | Calculated Property |
| Pvap | 90.37 | kPa | 574.01 | Calculated Property |
| Pvap | 137.42 | kPa | 592.12 | Calculated Property |
| Pvap | 202.67 | kPa | 610.23 | Calculated Property |
| Pvap | [9.05e-06; 1179.96] | kPa | [290.76; 739.26] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.27202e+02 | |||
| Coefficient B | -1.53670e+04 | |||
| Coefficient C | -1.51550e+01 | |||
| Coefficient D | 4.69670e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 748 K. | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 739.26 | |||
| Pvap | 9.05e-06 | kPa | 290.76 | Calculated Property |
| Pvap | 1.89e-03 | kPa | 340.59 | Calculated Property |
| Pvap | 0.08 | kPa | 390.43 | Calculated Property |
| Pvap | 1.08 | kPa | 440.26 | Calculated Property |
| Pvap | 7.64 | kPa | 490.09 | Calculated Property |
| Pvap | 33.47 | kPa | 539.93 | Calculated Property |
| Pvap | 105.52 | kPa | 589.76 | Calculated Property |
| Pvap | 266.04 | kPa | 639.59 | Calculated Property |
| Pvap | 581.77 | kPa | 689.43 | Calculated Property |
| Pvap | 1179.96 | kPa | 739.26 | Calculated Property |
| Pvap | [3.14e-06; 1376.33] | kPa | [290.76; 748.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.79261e+02 | |||
| Coefficient B | -2.28693e+04 | |||
| Coefficient C | -3.78359e+01 | |||
| Coefficient D | 1.59356e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 748.00 | |||
| Pvap | 3.14e-06 | kPa | 290.76 | Calculated Property |
| Pvap | 1.43e-03 | kPa | 341.56 | Calculated Property |
| Pvap | 0.08 | kPa | 392.37 | Calculated Property |
| Pvap | 1.24 | kPa | 443.17 | Calculated Property |
| Pvap | 8.81 | kPa | 493.98 | Calculated Property |
| Pvap | 37.73 | kPa | 544.78 | Calculated Property |
| Pvap | 116.86 | kPa | 595.59 | Calculated Property |
| Pvap | 295.10 | kPa | 646.39 | Calculated Property |
| Pvap | 658.85 | kPa | 697.20 | Calculated Property |
| Pvap | 1376.33 | kPa | 748.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [787.28; 329.20] | kg/m3 | [290.76; 739.26] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 4.93520e+01 | |||
| Coefficient B | 2.27180e-01 | |||
| Coefficient C | 7.48000e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 748 K. | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 739.26 | |||
| ρl | 787.28 | kg/m3 | 290.76 | Calculated Property |
| ρl | 755.08 | kg/m3 | 340.59 | Calculated Property |
| ρl | 721.43 | kg/m3 | 390.43 | Calculated Property |
| ρl | 685.99 | kg/m3 | 440.26 | Calculated Property |
| ρl | 648.24 | kg/m3 | 490.09 | Calculated Property |
| ρl | 607.42 | kg/m3 | 539.93 | Calculated Property |
| ρl | 562.20 | kg/m3 | 589.76 | Calculated Property |
| ρl | 510.02 | kg/m3 | 639.59 | Calculated Property |
| ρl | 444.43 | kg/m3 | 689.43 | Calculated Property |
| ρl | 329.20 | kg/m3 | 739.26 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [290.76; 739.26] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 5.75410e-02 | |||
| Coefficient B | 1.41070e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 1.00000e-07 | |||
| Critical temperature, Tc (K) | 7.39260e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 748 K. | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 739.26 | |||
| γ | 0.03 | N/m | 290.76 | Calculated Property |
| γ | 0.02 | N/m | 340.59 | Calculated Property |
| γ | 0.02 | N/m | 390.43 | Calculated Property |
| γ | 0.02 | N/m | 440.26 | Calculated Property |
| γ | 0.01 | N/m | 490.09 | Calculated Property |
| γ | 0.01 | N/m | 539.93 | Calculated Property |
| γ | 0.01 | N/m | 589.76 | Calculated Property |
| γ | 0.00 | N/m | 639.59 | Calculated Property |
| γ | 0.00 | N/m | 689.43 | Calculated Property |
| γ | 0.00 | N/m | 739.26 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.07] | W/m×K | [573.48; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.26760e-07 | |||
| Coefficient B | 1.90850e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 573.48 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 573.48 | Calculated Property |
| λgas | 0.03 | W/m×K | 620.87 | Calculated Property |
| λgas | 0.03 | W/m×K | 668.26 | Calculated Property |
| λgas | 0.04 | W/m×K | 715.65 | Calculated Property |
| λgas | 0.04 | W/m×K | 763.04 | Calculated Property |
| λgas | 0.05 | W/m×K | 810.44 | Calculated Property |
| λgas | 0.05 | W/m×K | 857.83 | Calculated Property |
| λgas | 0.06 | W/m×K | 905.22 | Calculated Property |
| λgas | 0.06 | W/m×K | 952.61 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.09] | W/m×K | [290.76; 587.97] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.03240e-01 | |||
| Coefficient B | -1.99570e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 290.76 | |||
| Temperature range, max. | 587.97 | |||
| λliquid | 0.15 | W/m×K | 290.76 | Calculated Property |
| λliquid | 0.14 | W/m×K | 323.78 | Calculated Property |
| λliquid | 0.13 | W/m×K | 356.81 | Calculated Property |
| λliquid | 0.13 | W/m×K | 389.83 | Calculated Property |
| λliquid | 0.12 | W/m×K | 422.85 | Calculated Property |
| λliquid | 0.11 | W/m×K | 455.88 | Calculated Property |
| λliquid | 0.11 | W/m×K | 488.90 | Calculated Property |
| λliquid | 0.10 | W/m×K | 521.92 | Calculated Property |
| λliquid | 0.09 | W/m×K | 554.95 | Calculated Property |
| λliquid | 0.09 | W/m×K | 587.97 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-Octadecene.
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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