- InChI
- InChI=1S/C15H32O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14-15-16/h16H,2-15H2,1H3
- InChI Key
- REIUXOLGHVXAEO-UHFFFAOYSA-N
- Formula
- C15H32O
- SMILES
- CCCCCCCCCCCCCCCO
- Molecular Weight1
- 228.41
- CAS
- 629-76-5
- Other Names
-
- 1-pentadecanol
- N-PENTADECYL ALCOHOL
- Neodol 5
- Pentadecan-1-ol
- n-1-Pentadecanol
- pentadecanol
- pentadecyl alcohol
- ω : Acentric Factor.
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid 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).
- ΔfH°solid : Solid phase 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (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 | [0.7507; 1.0150] |
|
|
| ω | 0.8072 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.7507 | ChemSep v8.3 pure component data Compiled value | |
| ω | 1.0150 | KDB | |
| ΔcH°solid | -9817.70 | kJ/mol | NIST |
| μ | 1.65 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -58.07 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -501.20 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°solid | -658.30 ± 0.60 | kJ/mol | NIST |
| ΔfusH° | [21.40; 103.50] | kJ/mol |
|
| ΔfusH° | 21.40 | kJ/mol | Heat capacities and derived thermodynamic functions of 1-dodecanol and 1-tridecanol between 10 K and 370 K and heat capacities of 1-pentadecanol and 1-heptadecanol between 300 K and 380 K and correlationos for the heat capacity and the entropy of liquid n-alcohols |
| ΔfusH° | 103.50 | kJ/mol | Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography |
| ΔvapH° | [102.50; 107.20] | kJ/mol |
|
| ΔvapH° | 103.50 ± 3.30 | kJ/mol | NIST |
| ΔvapH° | 102.50 | kJ/mol | NIST |
| ΔvapH° | 107.20 | kJ/mol | NIST |
| IE | 10.00 | eV | Relay (1.0) Calculated Property |
| log10WS | [-6.35; -6.35] |
|
|
| log10WS | -6.35 | Aq. Solubility Prediction | |
| log10WS | -6.35 | Estimated Solubility | |
| logPoct/wat | 5.070 | Crippen Calculated Property | |
| McVol | 228.080 | ml/mol | McGowan Calculated Property |
| Pc | [1520.00; 1599.92] | kPa |
|
| Pc | 1599.92 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 1569.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 1520.00 | kPa | KDB |
| Ptriple | 6.80e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [296.98; 1794.00] |
|
|
| Inp | 1765.10 | NIST | |
| Inp | 1777.00 | NIST | |
| Inp | 1732.00 | NIST | |
| Inp | 1776.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1772.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1787.00 | NIST | |
| Inp | 1788.90 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Inp | 1787.00 | NIST | |
| Inp | 1749.00 | NIST | |
| Inp | 1787.00 | NIST | |
| Inp | 1775.00 | NIST | |
| Inp | 1754.00 | NIST | |
| Inp | 1773.00 | NIST | |
| Inp | 1780.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1761.00 | NIST | |
| Inp | 1768.00 | NIST | |
| Inp | 1792.00 | NIST | |
| Inp | 1765.00 | NIST | |
| Inp | 1766.00 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1755.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | 1771.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Inp | 1778.00 | NIST | |
| Inp | 1789.00 | NIST | |
| Inp | Outlier 296.98 | NIST | |
| Inp | Outlier 298.56 | NIST | |
| Inp | 1791.00 | NIST | |
| Inp | 1765.10 | NIST | |
| Inp | 1794.00 | NIST | |
| Inp | 1774.00 | NIST | |
| Ip | [2241.00; 2287.00] |
|
|
| Ip | 2241.00 | NIST | |
| Ip | 2278.00 | NIST | |
| Ip | 2250.00 | NIST | |
| Ip | 2254.00 | NIST | |
| Ip | 2257.00 | NIST | |
| Ip | 2272.00 | NIST | |
| Ip | 2286.00 | NIST | |
| Ip | 2243.00 | NIST | |
| Ip | 2279.00 | NIST | |
| Ip | 2287.00 | NIST | |
| Ip | 2287.00 | NIST | |
| Ip | 2254.00 | NIST | |
| Ip | 2272.00 | NIST | |
| Tboil | [578.00; 583.90] | K |
|
| Tboil | 583.90 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 578.00 | K | KDB |
| Tc | [722.50; 757.30] | K |
|
| Tc | 757.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 757.30 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 722.50 | K | KDB |
| Tfus | [311.70; 319.15] | K |
|
| Tfus | 319.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 317.05 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 317.00 | K | KDB |
| Tfus | 318.98 | K | Aq. Solubility Prediction |
| Tfus | 317.65 ± 0.40 | K | NIST |
| Tfus | Outlier 311.70 ± 2.00 | K | NIST |
| Tfus | 316.92 ± 0.05 | K | NIST |
| Tfus | 316.61 ± 0.05 | K | NIST |
| Tfus | 316.92 ± 0.05 | K | NIST |
| Tfus | 316.61 ± 0.05 | K | NIST |
| Ttriple | 317.05 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 9.61 | ChemSep v8.3 pure component data Compiled value | |
| URi | 11.34 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.882; 1.010] | m3/kmol |
|
| Vc | 0.882 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 1.010 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.894 | m3/kmol | KDB |
| Zc | [0.2263340; 0.2510000] |
|
|
| Zc | 0.2510000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2263340 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | 567.40 | J/mol×K | 323.15 | NIST |
| Cp,solid | [400.00; 537.30] | J/mol×K | [298.15; 358.00] |
|
| Cp,solid | 400.00 | J/mol×K | 298.15 | NIST |
| Cp,solid | 535.00 | J/mol×K | 318.00 | NIST |
| Cp,solid | 537.30 | J/mol×K | 358.00 | NIST |
| ΔfusH | [23.64; 54.73] | kJ/mol | [316.00; 316.90] |
|
| ΔfusH | 23.64 | kJ/mol | 316.00 | NIST |
| ΔfusH | 29.60 | kJ/mol | 316.40 | NIST |
| ΔfusH | 54.73 | kJ/mol | 316.60 | NIST |
| ΔfusH | 54.73 | kJ/mol | 316.60 | NIST |
| ΔfusH | 54.73 | kJ/mol | 316.60 | NIST |
| ΔfusH | 53.62 | kJ/mol | 316.90 | NIST |
| ΔvapH | [72.40; 95.50] | kJ/mol | [338.50; 519.00] |
|
| ΔvapH | 95.50 | kJ/mol | 338.50 | NIST |
| ΔvapH | 92.40 | kJ/mol | 368.00 | NIST |
| ΔvapH | 72.40 | kJ/mol | 518.50 | NIST |
| ΔvapH | 75.00 | kJ/mol | 519.00 | NIST |
| ΔfusS | [74.81; 172.86] | J/mol×K | [316.00; 316.60] |
|
| ΔfusS | 74.81 | J/mol×K | 316.00 | NIST |
| ΔfusS | 172.86 | J/mol×K | 316.60 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [356.57; 902.85] | J/mol×K | [298.15; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·((C/T)/sinh(C/T))² + D·((E/T)/cosh(E/T))² Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 2.49400e+02 | |||
| Coefficient B | 7.74000e+02 | |||
| Coefficient C | 1.56400e+03 | |||
| Coefficient D | 5.80500e+02 | |||
| Coefficient E | 7.24100e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 356.57 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 491.41 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 597.14 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 677.48 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 739.95 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 789.03 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 827.76 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 858.49 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 883.05 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 902.85 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [562.98; 730.08] | J/mol×K | [317.05; 583.90] |
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 | -1.79690e+03 | |||
| Coefficient B | 1.50530e+01 | |||
| Coefficient C | -3.06950e-02 | |||
| Coefficient D | 2.11110e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 583.90 | |||
| Cp,liquid | 562.98 | J/mol×K | 317.05 | Calculated Property |
| Cp,liquid | 612.18 | J/mol×K | 346.70 | Calculated Property |
| Cp,liquid | 646.02 | J/mol×K | 376.35 | Calculated Property |
| Cp,liquid | 667.80 | J/mol×K | 406.00 | Calculated Property |
| Cp,liquid | 680.82 | J/mol×K | 435.65 | Calculated Property |
| Cp,liquid | 688.38 | J/mol×K | 465.30 | Calculated Property |
| Cp,liquid | 693.78 | J/mol×K | 494.95 | Calculated Property |
| Cp,liquid | 700.33 | J/mol×K | 524.60 | Calculated Property |
| Cp,liquid | 711.33 | J/mol×K | 554.25 | Calculated Property |
| Cp,liquid | 730.08 | J/mol×K | 583.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0126674; 0.0002360] | Pa×s | [317.05; 583.90] |
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 | -7.08900e+01 | |||
| Coefficient B | 6.21470e+03 | |||
| Coefficient C | 8.14710e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 583.90 | |||
| η | 0.0126674 | Pa×s | 317.05 | Calculated Property |
| η | 0.0049088 | Pa×s | 346.70 | Calculated Property |
| η | 0.0023335 | Pa×s | 376.35 | Calculated Property |
| η | 0.0012960 | Pa×s | 406.00 | Calculated Property |
| η | 0.0008120 | Pa×s | 435.65 | Calculated Property |
| η | 0.0005594 | Pa×s | 465.30 | Calculated Property |
| η | 0.0004157 | Pa×s | 494.95 | Calculated Property |
| η | 0.0003284 | Pa×s | 524.60 | Calculated Property |
| η | 0.0002728 | Pa×s | 554.25 | Calculated Property |
| η | 0.0002360 | Pa×s | 583.90 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [99.73; 0.00] | kJ/mol | [317.05; 757.30] |
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 | 1.00600e+02 | |||
| Coefficient B | -1.36400e+00 | |||
| Coefficient C | 4.47600e+00 | |||
| Coefficient D | -2.81800e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.57300e+02 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 757.30 | |||
| ΔvapH | 99.73 | kJ/mol | 317.05 | Calculated Property |
| ΔvapH | 91.66 | kJ/mol | 365.97 | Calculated Property |
| ΔvapH | 82.99 | kJ/mol | 414.88 | Calculated Property |
| ΔvapH | 74.26 | kJ/mol | 463.80 | Calculated Property |
| ΔvapH | 65.87 | kJ/mol | 512.72 | Calculated Property |
| ΔvapH | 58.10 | kJ/mol | 561.63 | Calculated Property |
| ΔvapH | 51.08 | kJ/mol | 610.55 | Calculated Property |
| ΔvapH | 44.66 | kJ/mol | 659.47 | Calculated Property |
| ΔvapH | 37.81 | kJ/mol | 708.38 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 757.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [453.72; 600.57] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.72985e+01 | |||
| Coefficient B | -5.96038e+03 | |||
| Coefficient C | -1.03335e+02 | |||
| Temperature range, min. | 453.72 | |||
| Temperature range, max. | 600.57 | |||
| Pvap | 1.33 | kPa | 453.72 | Calculated Property |
| Pvap | 2.84 | kPa | 470.04 | Calculated Property |
| Pvap | 5.68 | kPa | 486.35 | Calculated Property |
| Pvap | 10.73 | kPa | 502.67 | Calculated Property |
| Pvap | 19.27 | kPa | 518.99 | Calculated Property |
| Pvap | 33.13 | kPa | 535.30 | Calculated Property |
| Pvap | 54.74 | kPa | 551.62 | Calculated Property |
| Pvap | 87.32 | kPa | 567.94 | Calculated Property |
| Pvap | 134.94 | kPa | 584.25 | Calculated Property |
| Pvap | 202.65 | kPa | 600.57 | Calculated Property |
| Pvap | [6.82e-05; 1573.23] | kPa | [317.05; 757.30] |
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 | 1.78202e+02 | |||
| Coefficient B | -1.90680e+04 | |||
| Coefficient C | -2.21670e+01 | |||
| Coefficient D | 6.88890e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 757.30 | |||
| Pvap | 6.82e-05 | kPa | 317.05 | Calculated Property |
| Pvap | 8.86e-03 | kPa | 365.97 | Calculated Property |
| Pvap | 0.26 | kPa | 414.88 | Calculated Property |
| Pvap | 2.90 | kPa | 463.80 | Calculated Property |
| Pvap | 16.80 | kPa | 512.72 | Calculated Property |
| Pvap | 62.27 | kPa | 561.63 | Calculated Property |
| Pvap | 170.91 | kPa | 610.55 | Calculated Property |
| Pvap | 387.24 | kPa | 659.47 | Calculated Property |
| Pvap | 791.08 | kPa | 708.38 | Calculated Property |
| Pvap | 1573.23 | kPa | 757.30 | Calculated Property |
| Pvap | [0.93; 143.64] | kPa | [438.15; 600.15] |
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 | 2.55623e+02 | |||
| Coefficient B | -2.20313e+04 | |||
| Coefficient C | -3.41892e+01 | |||
| Coefficient D | 1.32387e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 438.15 | |||
| Temperature range, max. | 600.15 | |||
| Pvap | 0.93 | kPa | 438.15 | Calculated Property |
| Pvap | 2.11 | kPa | 456.15 | Calculated Property |
| Pvap | 4.38 | kPa | 474.15 | Calculated Property |
| Pvap | 8.44 | kPa | 492.15 | Calculated Property |
| Pvap | 15.23 | kPa | 510.15 | Calculated Property |
| Pvap | 25.96 | kPa | 528.15 | Calculated Property |
| Pvap | 42.17 | kPa | 546.15 | Calculated Property |
| Pvap | 65.68 | kPa | 564.15 | Calculated Property |
| Pvap | 98.65 | kPa | 582.15 | Calculated Property |
| Pvap | 143.64 | kPa | 600.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [823.34; 239.98] | kg/m3 | [317.05; 757.30] |
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 | 5.68751e+01 | |||
| Coefficient B | 2.37000e-01 | |||
| Coefficient C | 7.57300e+02 | |||
| Coefficient D | 2.86000e-01 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 757.30 | |||
| ρl | 823.34 | kg/m3 | 317.05 | Calculated Property |
| ρl | 790.39 | kg/m3 | 365.97 | Calculated Property |
| ρl | 755.87 | kg/m3 | 414.88 | Calculated Property |
| ρl | 719.38 | kg/m3 | 463.80 | Calculated Property |
| ρl | 680.35 | kg/m3 | 512.72 | Calculated Property |
| ρl | 637.90 | kg/m3 | 561.63 | Calculated Property |
| ρl | 590.50 | kg/m3 | 610.55 | Calculated Property |
| ρl | 535.06 | kg/m3 | 659.47 | Calculated Property |
| ρl | 463.21 | kg/m3 | 708.38 | Calculated Property |
| ρl | 239.98 | kg/m3 | 757.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [317.05; 757.30] |
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 | 6.90000e-02 | |||
| Coefficient B | 1.79300e+00 | |||
| Coefficient C | -5.34000e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.57300e+02 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 757.30 | |||
| γ | 0.03 | N/m | 317.05 | Calculated Property |
| γ | 0.03 | N/m | 365.97 | Calculated Property |
| γ | 0.02 | N/m | 414.88 | Calculated Property |
| γ | 0.02 | N/m | 463.80 | Calculated Property |
| γ | 0.01 | N/m | 512.72 | Calculated Property |
| γ | 0.01 | N/m | 561.63 | Calculated Property |
| γ | 0.01 | N/m | 610.55 | Calculated Property |
| γ | 0.00 | N/m | 659.47 | Calculated Property |
| γ | 0.00 | N/m | 708.38 | Calculated Property |
| γ | 0.00 | N/m | 757.30 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.08] | W/m×K | [583.90; 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 | -2.70700e+00 | |||
| Coefficient B | -2.80240e-02 | |||
| Coefficient C | -1.92660e+03 | |||
| Coefficient D | -2.76990e+07 | |||
| Temperature range, min. | 583.90 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 583.90 | Calculated Property |
| λgas | 0.03 | W/m×K | 630.13 | Calculated Property |
| λgas | 0.04 | W/m×K | 676.37 | Calculated Property |
| λgas | 0.04 | W/m×K | 722.60 | Calculated Property |
| λgas | 0.05 | W/m×K | 768.83 | Calculated Property |
| λgas | 0.05 | W/m×K | 815.07 | Calculated Property |
| λgas | 0.06 | W/m×K | 861.30 | Calculated Property |
| λgas | 0.06 | W/m×K | 907.53 | Calculated Property |
| λgas | 0.07 | W/m×K | 953.77 | Calculated Property |
| λgas | 0.08 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.16; 0.10] | W/m×K | [317.05; 583.90] |
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 | 2.29330e-01 | |||
| Coefficient B | -2.22710e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 317.05 | |||
| Temperature range, max. | 583.90 | |||
| λliquid | 0.16 | W/m×K | 317.05 | Calculated Property |
| λliquid | 0.15 | W/m×K | 346.70 | Calculated Property |
| λliquid | 0.15 | W/m×K | 376.35 | Calculated Property |
| λliquid | 0.14 | W/m×K | 406.00 | Calculated Property |
| λliquid | 0.13 | W/m×K | 435.65 | Calculated Property |
| λliquid | 0.13 | W/m×K | 465.30 | Calculated Property |
| λliquid | 0.12 | W/m×K | 494.95 | Calculated Property |
| λliquid | 0.11 | W/m×K | 524.60 | Calculated Property |
| λliquid | 0.11 | W/m×K | 554.25 | Calculated Property |
| λliquid | 0.10 | W/m×K | 583.90 | Calculated Property |
Similar Compounds
Find more compounds similar to n-Pentadecanol.
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).
- 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
- Heat capacities and derived thermodynamic functions of 1-dodecanol and 1-tridecanol between 10 K and 370 K and heat capacities of 1-pentadecanol and 1-heptadecanol between 300 K and 380 K and correlationos for the heat capacity and the entropy of liquid n-alcohols
- Evaluation of the Vaporization, Fusion, and Sublimation Enthalpies of the 1-Alkanols: The Vaporization Enthalpy of 1-, 6-, 7-, and 9-Heptadecanol, 1-Octadecanol, 1-Eicosanol, 1-Docosanol, 1-Hexacosanol, and Cholesterol at T ) 298.15 K by Correlation Gas Chromatography
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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