- InChI
- InChI=1S/C13H26O/c1-2-3-4-5-6-7-8-9-10-11-12-13-14/h13H,2-12H2,1H3
- InChI Key
- BGEHHAVMRVXCGR-UHFFFAOYSA-N
- Formula
- C13H26O
- SMILES
- CCCCCCCCCCCCC=O
- Molecular Weight1
- 198.34
- CAS
- 10486-19-8
- Other Names
-
- 1-Tridecanal
- Tridecanaldehyde
- Tridecane aldehyde
- Tridecyl aldehyde
- n-Tridecanal
- n-Tridecylaldehyde
- ω : Acentric Factor.
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid 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).
- 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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (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 | 0.7161 | ChemSep v8.3 pure component data Compiled value | |
| μ | 2.58 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -42.98 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -392.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 31.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 73.30 ± 0.40 | kJ/mol | NIST |
| IE | 9.63 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.29 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.496 | Crippen Calculated Property | |
| McVol | 195.600 | ml/mol | McGowan Calculated Property |
| Pc | 1740.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.26e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [277.00; 1531.00] |
|
|
| Inp | 1525.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1489.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | 1494.00 | NIST | |
| Inp | 1531.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1511.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1511.00 | NIST | |
| Inp | 1486.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1511.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1506.00 | NIST | |
| Inp | 1504.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1501.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1508.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1495.00 | NIST | |
| Inp | 1509.00 | NIST | |
| Inp | 1506.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1497.00 | NIST | |
| Inp | 1505.00 | NIST | |
| Inp | 1496.00 | NIST | |
| Inp | 1484.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1506.00 | NIST | |
| Inp | 1507.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1483.00 | NIST | |
| Inp | 1483.00 | NIST | |
| Inp | 1513.00 | NIST | |
| Inp | 1493.00 | NIST | |
| Inp | 1495.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1519.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1495.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1495.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1514.00 | NIST | |
| Inp | 1516.00 | NIST | |
| Inp | 1524.00 | NIST | |
| Inp | 1524.00 | NIST | |
| Inp | 1522.00 | NIST | |
| Inp | 1523.00 | NIST | |
| Inp | 1496.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1517.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1510.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1524.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Inp | 1523.00 | NIST | |
| Inp | 1486.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | Outlier 277.00 | NIST | |
| Inp | 1508.00 | NIST | |
| Inp | 1509.00 | NIST | |
| Inp | 1491.00 | NIST | |
| Inp | 1512.00 | NIST | |
| Inp | 1488.00 | NIST | |
| Inp | 1493.00 | NIST | |
| Inp | 1490.00 | NIST | |
| Inp | 1531.00 | NIST | |
| Inp | 1503.00 | NIST | |
| Inp | 1492.00 | NIST | |
| Inp | 1525.00 | NIST | |
| Inp | 1518.00 | NIST | |
| Ip | [1782.00; 1844.00] |
|
|
| Ip | 1803.00 | NIST | |
| Ip | 1822.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | 1792.00 | NIST | |
| Ip | 1809.00 | NIST | |
| Ip | 1822.00 | NIST | |
| Ip | 1811.00 | NIST | |
| Ip | 1821.00 | NIST | |
| Ip | 1816.00 | NIST | |
| Ip | 1833.00 | NIST | |
| Ip | 1844.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | Outlier 1784.00 | NIST | |
| Ip | 1805.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1800.00 | NIST | |
| Ip | 1824.00 | NIST | |
| Ip | Outlier 1782.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1794.00 | NIST | |
| Ip | 1800.00 | NIST | |
| Ip | 1844.00 | NIST | |
| Ip | 1830.00 | NIST | |
| Ip | 1833.00 | NIST | |
| Ip | 1800.00 | NIST | |
| Tboil | [540.15; 553.15] | K |
|
| Tboil | 540.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 553.15 ± 5.00 | K | NIST |
| Tc | 700.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [287.00; 288.15] | K |
|
| Tfus | 287.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 288.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 288.00 ± 3.00 | K | NIST |
| Tfus | 287.00 ± 3.00 | K | NIST |
| Ttriple | 288.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 7.74 | ChemSep v8.3 pure component data Compiled value | |
| URi | 9.32 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.738 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2880000 | ChemSep v8.3 pure component data Compiled value |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 407.20 | K | 1.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [308.31; 781.12] | 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 | 2.32640e+02 | |||
| Coefficient B | 6.72160e+02 | |||
| Coefficient C | 1.62170e+03 | |||
| Coefficient D | 4.45650e+02 | |||
| Coefficient E | 7.45040e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 308.31 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 411.46 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 497.56 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 567.02 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 623.67 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 669.71 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 706.94 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 737.00 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 761.32 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 781.12 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [414.46; 580.08] | J/mol×K | [298.15; 540.15] |
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 | 2.10410e+02 | |||
| Coefficient B | 6.84380e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 540.15 | |||
| Cp,liquid | 414.46 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 432.86 | J/mol×K | 325.04 | Calculated Property |
| Cp,liquid | 451.26 | J/mol×K | 351.93 | Calculated Property |
| Cp,liquid | 469.66 | J/mol×K | 378.82 | Calculated Property |
| Cp,liquid | 488.07 | J/mol×K | 405.71 | Calculated Property |
| Cp,liquid | 506.47 | J/mol×K | 432.59 | Calculated Property |
| Cp,liquid | 524.87 | J/mol×K | 459.48 | Calculated Property |
| Cp,liquid | 543.27 | J/mol×K | 486.37 | Calculated Property |
| Cp,liquid | 561.68 | J/mol×K | 513.26 | Calculated Property |
| Cp,liquid | 580.08 | J/mol×K | 540.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0023602; 0.0003857] | Pa×s | [288.15; 540.15] |
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 | -9.98470e+00 | |||
| Coefficient B | 1.12170e+03 | |||
| Coefficient C | 7.58050e-03 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 540.15 | |||
| η | 0.0023602 | Pa×s | 288.15 | Calculated Property |
| η | 0.0016731 | Pa×s | 316.15 | Calculated Property |
| η | 0.0012544 | Pa×s | 344.15 | Calculated Property |
| η | 0.0009822 | Pa×s | 372.15 | Calculated Property |
| η | 0.0007959 | Pa×s | 400.15 | Calculated Property |
| η | 0.0006629 | Pa×s | 428.15 | Calculated Property |
| η | 0.0005647 | Pa×s | 456.15 | Calculated Property |
| η | 0.0004901 | Pa×s | 484.15 | Calculated Property |
| η | 0.0004319 | Pa×s | 512.15 | Calculated Property |
| η | 0.0003857 | Pa×s | 540.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [76.53; 0.00] | kJ/mol | [288.15; 700.00] |
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 | 9.61850e+01 | |||
| Coefficient B | 4.31020e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.00000e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 724 K. | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 700.00 | |||
| ΔvapH | 76.53 | kJ/mol | 288.15 | Calculated Property |
| ΔvapH | 72.74 | kJ/mol | 333.91 | Calculated Property |
| ΔvapH | 68.67 | kJ/mol | 379.67 | Calculated Property |
| ΔvapH | 64.26 | kJ/mol | 425.43 | Calculated Property |
| ΔvapH | 59.40 | kJ/mol | 471.19 | Calculated Property |
| ΔvapH | 53.95 | kJ/mol | 516.96 | Calculated Property |
| ΔvapH | 47.66 | kJ/mol | 562.72 | Calculated Property |
| ΔvapH | 40.02 | kJ/mol | 608.48 | Calculated Property |
| ΔvapH | 29.68 | kJ/mol | 654.24 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 700.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [414.62; 587.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47256e+01 | |||
| Coefficient B | -4.66793e+03 | |||
| Coefficient C | -9.13120e+01 | |||
| Temperature range, min. | 414.62 | |||
| Temperature range, max. | 587.15 | |||
| Pvap | 1.33 | kPa | 414.62 | Calculated Property |
| Pvap | 2.99 | kPa | 433.79 | Calculated Property |
| Pvap | 6.16 | kPa | 452.96 | Calculated Property |
| Pvap | 11.80 | kPa | 472.13 | Calculated Property |
| Pvap | 21.23 | kPa | 491.30 | Calculated Property |
| Pvap | 36.20 | kPa | 510.47 | Calculated Property |
| Pvap | 58.92 | kPa | 529.64 | Calculated Property |
| Pvap | 92.06 | kPa | 548.81 | Calculated Property |
| Pvap | 138.76 | kPa | 567.98 | Calculated Property |
| Pvap | 202.63 | kPa | 587.15 | Calculated Property |
| Pvap | [1.26e-04; 2349.72] | kPa | [288.15; 724.00] |
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 | 3.35572e+02 | |||
| Coefficient B | -2.11870e+04 | |||
| Coefficient C | -5.00220e+01 | |||
| Coefficient D | 4.25940e-02 | |||
| Coefficient E | 1.00000e+00 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 724.00 | |||
| Pvap | 1.26e-04 | kPa | 288.15 | Calculated Property |
| Pvap | 0.02 | kPa | 336.58 | Calculated Property |
| Pvap | 0.43 | kPa | 385.01 | Calculated Property |
| Pvap | 4.19 | kPa | 433.43 | Calculated Property |
| Pvap | 22.39 | kPa | 481.86 | Calculated Property |
| Pvap | 81.17 | kPa | 530.29 | Calculated Property |
| Pvap | 228.42 | kPa | 578.72 | Calculated Property |
| Pvap | 545.12 | kPa | 627.14 | Calculated Property |
| Pvap | 1169.88 | kPa | 675.57 | Calculated Property |
| Pvap | 2349.72 | kPa | 724.00 | Calculated Property |
| Pvap | [1.18e-04; 1764.50] | kPa | [288.15; 700.00] |
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 | 2.45197e+02 | |||
| Coefficient B | -1.91915e+04 | |||
| Coefficient C | -3.33820e+01 | |||
| Coefficient D | 1.71089e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 700.00 | |||
| Pvap | 1.18e-04 | kPa | 288.15 | Calculated Property |
| Pvap | 0.01 | kPa | 333.91 | Calculated Property |
| Pvap | 0.32 | kPa | 379.67 | Calculated Property |
| Pvap | 3.06 | kPa | 425.43 | Calculated Property |
| Pvap | 16.29 | kPa | 471.19 | Calculated Property |
| Pvap | 58.89 | kPa | 516.96 | Calculated Property |
| Pvap | 165.44 | kPa | 562.72 | Calculated Property |
| Pvap | 395.64 | kPa | 608.48 | Calculated Property |
| Pvap | 857.99 | kPa | 654.24 | Calculated Property |
| Pvap | 1764.50 | kPa | 700.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [833.88; 268.76] | kg/m3 | [288.15; 724.00] |
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 | 6.99464e+01 | |||
| Coefficient B | 2.60260e-01 | |||
| Coefficient C | 7.24000e+02 | |||
| Coefficient D | 3.40790e-01 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 724.00 | |||
| ρl | 833.88 | kg/m3 | 288.15 | Calculated Property |
| ρl | 797.55 | kg/m3 | 336.58 | Calculated Property |
| ρl | 759.88 | kg/m3 | 385.01 | Calculated Property |
| ρl | 720.51 | kg/m3 | 433.43 | Calculated Property |
| ρl | 678.96 | kg/m3 | 481.86 | Calculated Property |
| ρl | 634.41 | kg/m3 | 530.29 | Calculated Property |
| ρl | 585.51 | kg/m3 | 578.72 | Calculated Property |
| ρl | 529.53 | kg/m3 | 627.14 | Calculated Property |
| ρl | 459.12 | kg/m3 | 675.57 | Calculated Property |
| ρl | 268.76 | kg/m3 | 724.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.10] | W/m×K | [540.15; 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 | -1.69670e+00 | |||
| Coefficient B | 1.02620e-01 | |||
| Coefficient C | -3.08030e+03 | |||
| Coefficient D | -3.29630e+07 | |||
| Temperature range, min. | 540.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 540.15 | Calculated Property |
| λgas | 0.03 | W/m×K | 591.24 | Calculated Property |
| λgas | 0.04 | W/m×K | 642.34 | Calculated Property |
| λgas | 0.05 | W/m×K | 693.43 | Calculated Property |
| λgas | 0.05 | W/m×K | 744.53 | Calculated Property |
| λgas | 0.06 | W/m×K | 795.62 | Calculated Property |
| λgas | 0.07 | W/m×K | 846.72 | Calculated Property |
| λgas | 0.08 | W/m×K | 897.81 | Calculated Property |
| λgas | 0.09 | W/m×K | 948.91 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.09] | W/m×K | [288.15; 540.15] |
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 | 1.99020e-01 | |||
| Coefficient B | -2.00490e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 288.15 | |||
| Temperature range, max. | 540.15 | |||
| λliquid | 0.14 | W/m×K | 288.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 316.15 | Calculated Property |
| λliquid | 0.13 | W/m×K | 344.15 | Calculated Property |
| λliquid | 0.12 | W/m×K | 372.15 | Calculated Property |
| λliquid | 0.12 | W/m×K | 400.15 | Calculated Property |
| λliquid | 0.11 | W/m×K | 428.15 | Calculated Property |
| λliquid | 0.11 | W/m×K | 456.15 | Calculated Property |
| λliquid | 0.10 | W/m×K | 484.15 | Calculated Property |
| λliquid | 0.10 | W/m×K | 512.15 | Calculated Property |
| λliquid | 0.09 | W/m×K | 540.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Tridecanal.
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)
- 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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