- InChI
- InChI=1S/C19H40O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16-17-18-19-20/h20H,2-19H2,1H3
- InChI Key
- XGFDHKJUZCCPKQ-UHFFFAOYSA-N
- Formula
- C19H40O
- SMILES
- CCCCCCCCCCCCCCCCCCCO
- Molecular Weight1
- 284.52
- CAS
- 1454-84-8
- Other Names
-
- 1-Nonadecanol
- N-NONADECANOL
- N-NONADECYL ALCOHOL
- Nonadecan-1-ol
- Nonadecanol
- Nonadecyl alcohol
- 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).
- 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).
- 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.
- I : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 | 0.9760 | KDB | |
| ΔfG° | -27.72 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -587.72 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 49.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 74.57 | kJ/mol | Joback Calculated Property |
| log10WS | -7.04 | Crippen Calculated Property | |
| logPoct/wat | 6.630 | Crippen Calculated Property | |
| McVol | 284.440 | ml/mol | McGowan Calculated Property |
| Pc | 1150.00 | kPa | KDB |
| Inp | [2150.00; 2194.70] |
|
|
| Inp | 2176.00 | NIST | |
| Inp | 2176.00 | NIST | |
| Inp | 2150.00 | NIST | |
| Inp | 2181.00 | NIST | |
| Inp | 2162.00 | NIST | |
| Inp | 2150.00 | NIST | |
| Inp | 2160.00 | NIST | |
| Inp | 2150.00 | NIST | |
| Inp | 2176.00 | NIST | |
| Inp | 2156.00 | NIST | |
| Inp | Outlier 2194.70 | NIST | |
| Inp | 2172.00 | NIST | |
| Inp | 2175.00 | NIST | |
| Inp | 2153.00 | NIST | |
| Inp | 2153.00 | NIST | |
| I | [2637.00; 2687.00] |
|
|
| I | 2652.00 | NIST | |
| I | 2687.00 | NIST | |
| I | 2637.00 | NIST | |
| I | 2646.00 | NIST | |
| I | 2652.00 | NIST | |
| Tboil | 631.00 | K | KDB |
| Tc | 775.30 | K | KDB |
| Tfus | [333.00; 336.00] | K |
|
| Tfus | 335.00 | K | KDB |
| Tfus | 334.65 ± 0.50 | K | NIST |
| Tfus | 336.00 ± 4.00 | K | NIST |
| Tfus | 333.00 ± 4.00 | K | NIST |
| Vc | 1.119 | m3/kmol | KDB |
| Zc | 0.1995390 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [866.72; 966.74] | J/mol×K | [726.30; 892.39] |
|
| Cp,gas | 866.72 | J/mol×K | 726.30 | Joback Calculated Property |
| Cp,gas | 885.33 | J/mol×K | 753.98 | Joback Calculated Property |
| Cp,gas | 903.13 | J/mol×K | 781.66 | Joback Calculated Property |
| Cp,gas | 920.14 | J/mol×K | 809.35 | Joback Calculated Property |
| Cp,gas | 936.39 | J/mol×K | 837.03 | Joback Calculated Property |
| Cp,gas | 951.91 | J/mol×K | 864.71 | Joback Calculated Property |
| Cp,gas | 966.74 | J/mol×K | 892.39 | Joback Calculated Property |
| η | [0.0000237; 0.0043497] | Pa×s | [364.71; 726.30] |
|
| η | 0.0043497 | Pa×s | 364.71 | Joback Calculated Property |
| η | 0.0009853 | Pa×s | 424.97 | Joback Calculated Property |
| η | 0.0003227 | Pa×s | 485.24 | Joback Calculated Property |
| η | 0.0001353 | Pa×s | 545.50 | Joback Calculated Property |
| η | 0.0000674 | Pa×s | 605.77 | Joback Calculated Property |
| η | 0.0000381 | Pa×s | 666.03 | Joback Calculated Property |
| η | 0.0000237 | Pa×s | 726.30 | Joback Calculated Property |
| ΔfusH | [43.30; 72.42] | kJ/mol | [333.90; 334.50] |
|
| ΔfusH | 43.30 | kJ/mol | 333.90 | NIST |
| ΔfusH | 43.30 | kJ/mol | 333.90 | NIST |
| ΔfusH | 72.42 | kJ/mol | 334.50 | NIST |
| ΔvapH | [80.00; 81.70] | kJ/mol | [559.50; 564.50] |
|
| ΔvapH | 81.70 | kJ/mol | 559.50 | NIST |
| ΔvapH | 80.00 | kJ/mol | 564.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 439.70 | K | 0.04 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [492.60; 662.10] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.64486e+01 | |||
| Coefficient B | -6.07256e+03 | |||
| Coefficient C | -1.16846e+02 | |||
| Temperature range, min. | 492.60 | |||
| Temperature range, max. | 662.10 | |||
| Pvap | 1.33 | kPa | 492.60 | Calculated Property |
| Pvap | 2.88 | kPa | 511.43 | Calculated Property |
| Pvap | 5.81 | kPa | 530.27 | Calculated Property |
| Pvap | 11.02 | kPa | 549.10 | Calculated Property |
| Pvap | 19.82 | kPa | 567.93 | Calculated Property |
| Pvap | 33.99 | kPa | 586.77 | Calculated Property |
| Pvap | 55.93 | kPa | 605.60 | Calculated Property |
| Pvap | 88.68 | kPa | 624.43 | Calculated Property |
| Pvap | 136.05 | kPa | 643.27 | Calculated Property |
| Pvap | 202.65 | kPa | 662.10 | Calculated Property |
Similar Compounds
Find more compounds similar to n-Nonadecanol-1.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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