- InChI
- InChI=1S/C19H40O/c1-3-5-7-9-11-13-15-17-19(20)18-16-14-12-10-8-6-4-2/h19-20H,3-18H2,1-2H3
- InChI Key
- ACMBVSPXQQUNOF-UHFFFAOYSA-N
- Formula
- C19H40O
- SMILES
- CCCCCCCCCC(O)CCCCCCCCC
- Molecular Weight1
- 284.53
- CAS
- 16840-84-9
- Other Names
-
- nonadecan-10-ol
- 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).
- 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).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 1.0152 | Relay (1.0) Calculated Property | |
| ΔfG° | -30.16 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -610.38 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 45.53 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 118.12 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.87 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.79 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.629 | Crippen Calculated Property | |
| McVol | 284.440 | ml/mol | McGowan Calculated Property |
| Pc | 1155.35 | kPa | Joback Calculated Property |
| Tboil | 597.14 | K | Relay (1.0) Calculated Property |
| Tc | 772.51 | K | Relay (1.0) Calculated Property |
| Tfus | 329.05 | K | Relay (1.0) Calculated Property |
| Vc | 1.125 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [420.73; 1018.77] | 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 | -1.07740e+01 | |||
| Coefficient B | 1.84874e+00 | |||
| Coefficient C | -1.04340e-03 | |||
| Coefficient D | 2.24200e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 420.73 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 522.61 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 613.97 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 695.53 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 768.00 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 832.09 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 888.50 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 937.94 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 981.13 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 1018.77 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0066420; 0.0000515] | Pa×s | [349.71; 625.12] |
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 | -1.60432e+01 | |||
| Coefficient B | 3.85689e+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. | 349.71 | |||
| Temperature range, max. | 625.12 | |||
| η | 0.0066420 | Pa×s | 349.71 | Calculated Property |
| η | 0.0027347 | Pa×s | 380.31 | Calculated Property |
| η | 0.0012850 | Pa×s | 410.91 | Calculated Property |
| η | 0.0006705 | Pa×s | 441.51 | Calculated Property |
| η | 0.0003806 | Pa×s | 472.11 | Calculated Property |
| η | 0.0002315 | Pa×s | 502.71 | Calculated Property |
| η | 0.0001490 | Pa×s | 533.31 | Calculated Property |
| η | 0.0001007 | Pa×s | 563.91 | Calculated Property |
| η | 0.0000708 | Pa×s | 594.52 | Calculated Property |
| η | 0.0000515 | Pa×s | 625.12 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [481.36; 665.90] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53415e+01 | |||
| Coefficient B | -5.54614e+03 | |||
| Coefficient C | -1.12940e+02 | |||
| Temperature range, min. | 481.36 | |||
| Temperature range, max. | 665.90 | |||
| Pvap | 1.33 | kPa | 481.36 | Calculated Property |
| Pvap | 2.95 | kPa | 501.86 | Calculated Property |
| Pvap | 6.02 | kPa | 522.37 | Calculated Property |
| Pvap | 11.49 | kPa | 542.87 | Calculated Property |
| Pvap | 20.67 | kPa | 563.38 | Calculated Property |
| Pvap | 35.33 | kPa | 583.88 | Calculated Property |
| Pvap | 57.75 | kPa | 604.39 | Calculated Property |
| Pvap | 90.75 | kPa | 624.89 | Calculated Property |
| Pvap | 137.73 | kPa | 645.40 | Calculated Property |
| Pvap | 202.66 | kPa | 665.90 | Calculated Property |
Similar Compounds
Find more compounds similar to 10-Nonadecanol.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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