- 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).
- 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.
- 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).
- 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 | [0.8600; 0.9760] |
|
|
| ω | 0.8600 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.9760 | KDB | |
| ΔfG° | -21.83 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -587.72 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 49.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 127.93 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.12 | eV | Relay (1.0) Calculated Property |
| log10WS | -7.28 | Relay (1.0) Calculated Property | |
| logPoct/wat | 6.630 | Crippen Calculated Property | |
| McVol | 284.440 | ml/mol | McGowan Calculated Property |
| Pc | [1142.84; 1150.00] | kPa |
|
| Pc | 1142.84 | kPa | ChemSep v8.3 pure component data Compiled value |
| 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 | 2150.00 | NIST | |
| Inp | 2153.00 | NIST | |
| Inp | 2176.00 | 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 | [624.00; 631.00] | K |
|
| Tboil | 624.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 631.00 | K | KDB |
| Tc | [775.30; 795.00] | K |
|
| Tc | 795.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 775.30 | K | KDB |
| Tfus | [333.00; 336.00] | K |
|
| Tfus | 335.15 | K | ChemSep v8.3 pure component data Compiled value |
| 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 |
| UQi | 11.77 | ChemSep v8.3 pure component data Compiled value | |
| URi | 14.04 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [1.113; 1.119] | m3/kmol |
|
| Vc | 1.113 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 1.119 | m3/kmol | KDB |
| Zc | [0.1924920; 0.1995390] |
|
|
| Zc | 0.1924920 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.1995390 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| 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 |
|---|---|---|---|---|
| Cp,gas | [372.44; 1127.06] | J/mol×K | [255.00; 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 | 1.87973e+02 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 7.17824e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 372.44 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 555.60 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 699.71 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 809.37 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 894.02 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 960.82 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 1014.65 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 1058.87 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 1095.79 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 1127.06 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0111003; 0.0001284] | Pa×s | [334.76; 549.60] |
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 | -1.59092e+01 | |||
| Coefficient B | 3.81907e+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. | 334.76 | |||
| Temperature range, max. | 549.60 | |||
| η | 0.0111003 | Pa×s | 334.76 | Calculated Property |
| η | 0.0051945 | Pa×s | 358.63 | Calculated Property |
| η | 0.0026725 | Pa×s | 382.50 | Calculated Property |
| η | 0.0014866 | Pa×s | 406.37 | Calculated Property |
| η | 0.0008825 | Pa×s | 430.25 | Calculated Property |
| η | 0.0005535 | Pa×s | 454.12 | Calculated Property |
| η | 0.0003637 | Pa×s | 477.99 | Calculated Property |
| η | 0.0002487 | Pa×s | 501.86 | Calculated Property |
| η | 0.0001760 | Pa×s | 525.73 | Calculated Property |
| η | 0.0001284 | Pa×s | 549.60 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [492.60; 662.10] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| 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
- 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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