- InChI
- InChI=1S/C19H38/c1-3-5-7-9-11-13-15-17-19-18-16-14-12-10-8-6-4-2/h3H,1,4-19H2,2H3
- InChI Key
- NHLUYCJZUXOUBX-UHFFFAOYSA-N
- Formula
- C19H38
- SMILES
- C=CCCCCCCCCCCCCCCCCC
- Molecular Weight1
- 266.51
- CAS
- 18435-45-5
- Other Names
-
- Nonadec-1-ene
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- 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).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- 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 | 0.7470 | KDB | |
| ΔfG° | 196.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -325.11 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 43.69 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 95.00 | kJ/mol | NIST |
| IE | 9.60 | eV | Relay (1.0) Calculated Property |
| log10WS | -8.04 | Relay (1.0) Calculated Property | |
| logPoct/wat | 7.434 | Crippen Calculated Property | |
| McVol | 274.270 | ml/mol | McGowan Calculated Property |
| Pc | 1110.00 | kPa | KDB |
| Inp | [298.50; 1899.00] |
|
|
| Inp | 1899.00 | NIST | |
| Inp | 1891.00 | NIST | |
| Inp | 1883.00 | NIST | |
| Inp | 1885.00 | NIST | |
| Inp | 1892.00 | NIST | |
| Inp | 1895.00 | NIST | |
| Inp | 1883.00 | NIST | |
| Inp | 1883.00 | NIST | |
| Inp | 1894.00 | NIST | |
| Inp | 1899.00 | NIST | |
| Inp | 1880.00 | NIST | |
| Inp | 1890.00 | NIST | |
| Inp | 1892.00 | NIST | |
| Inp | 1891.00 | NIST | |
| Inp | 1885.00 | NIST | |
| Inp | 1892.00 | NIST | |
| Inp | 1893.00 | NIST | |
| Inp | 1881.00 | NIST | |
| Inp | 1891.00 | NIST | |
| Inp | 1890.00 | NIST | |
| Inp | 1894.00 | NIST | |
| Inp | 1890.00 | NIST | |
| Inp | 1892.00 | NIST | |
| Inp | 1875.00 | NIST | |
| Inp | Outlier 298.50 | NIST | |
| Inp | Outlier 298.50 | NIST | |
| Inp | 1883.00 | NIST | |
| Ip | [1920.00; 1960.00] |
|
|
| Ip | 1960.00 | NIST | |
| Ip | 1956.00 | NIST | |
| Ip | 1938.00 | NIST | |
| Ip | 1943.00 | NIST | |
| Ip | 1920.00 | NIST | |
| Tboil | 601.70 | K | KDB |
| Tc | 755.10 | K | KDB |
| Tfus | [296.15; 297.00] | K |
|
| Tfus | 296.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 297.00 | K | KDB |
| Vc | 1.107 | m3/kmol | KDB |
| Zc | 0.1956290 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [54.81; 63.30] | kJ/mol | [582.00; 601.70] |
|
| ΔvapH | 63.30 | kJ/mol | 582.00 | NIST |
| ΔvapH | 54.81 | kJ/mol | 601.70 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [398.73; 971.05] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -1.73740e+01 | |||
| Coefficient B | 1.78882e+00 | |||
| Coefficient C | -1.03270e-03 | |||
| Coefficient D | 2.32300e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 398.73 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 496.51 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 584.02 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 662.00 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 731.20 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 792.34 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 846.16 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 893.40 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 934.78 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 971.05 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0043343; 0.0002135] | Pa×s | [296.57; 528.57] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.23006e+01 | |||
| Coefficient B | 2.03432e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 296.57 | |||
| Temperature range, max. | 528.57 | |||
| η | 0.0043343 | Pa×s | 296.57 | Calculated Property |
| η | 0.0025044 | Pa×s | 322.35 | Calculated Property |
| η | 0.0015695 | Pa×s | 348.13 | Calculated Property |
| η | 0.0010491 | Pa×s | 373.91 | Calculated Property |
| η | 0.0007386 | Pa×s | 399.68 | Calculated Property |
| η | 0.0005426 | Pa×s | 425.46 | Calculated Property |
| η | 0.0004129 | Pa×s | 451.24 | Calculated Property |
| η | 0.0003236 | Pa×s | 477.02 | Calculated Property |
| η | 0.0002601 | Pa×s | 502.79 | Calculated Property |
| η | 0.0002135 | Pa×s | 528.57 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [457.75; 624.83] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.58056e+01 | |||
| Coefficient B | -5.41610e+03 | |||
| Coefficient C | -1.08726e+02 | |||
| Temperature range, min. | 457.75 | |||
| Temperature range, max. | 624.83 | |||
| Pvap | 1.33 | kPa | 457.75 | Calculated Property |
| Pvap | 2.92 | kPa | 476.31 | Calculated Property |
| Pvap | 5.93 | kPa | 494.88 | Calculated Property |
| Pvap | 11.28 | kPa | 513.44 | Calculated Property |
| Pvap | 20.29 | kPa | 532.01 | Calculated Property |
| Pvap | 34.73 | kPa | 550.57 | Calculated Property |
| Pvap | 56.94 | kPa | 569.14 | Calculated Property |
| Pvap | 89.83 | kPa | 587.70 | Calculated Property |
| Pvap | 136.98 | kPa | 606.27 | Calculated Property |
| Pvap | 202.63 | kPa | 624.83 | Calculated Property |
| Pvap | [4.04e-06; 1270.62] | kPa | [296.55; 760.00] |
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 | 2.16828e+02 | |||
| Coefficient B | -2.01039e+04 | |||
| Coefficient C | -2.85243e+01 | |||
| Coefficient D | 1.03581e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 296.55 | |||
| Temperature range, max. | 760.00 | |||
| Pvap | 4.04e-06 | kPa | 296.55 | Calculated Property |
| Pvap | 1.34e-03 | kPa | 348.04 | Calculated Property |
| Pvap | 0.07 | kPa | 399.54 | Calculated Property |
| Pvap | 1.04 | kPa | 451.03 | Calculated Property |
| Pvap | 7.59 | kPa | 502.53 | Calculated Property |
| Pvap | 33.99 | kPa | 554.02 | Calculated Property |
| Pvap | 109.43 | kPa | 605.52 | Calculated Property |
| Pvap | 282.24 | kPa | 657.01 | Calculated Property |
| Pvap | 628.09 | kPa | 708.51 | Calculated Property |
| Pvap | 1270.62 | kPa | 760.00 | Calculated Property |
Similar Compounds
Find more compounds similar to 1-NONADECENE.
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).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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