- InChI
- InChI=1S/C12H24O/c1-2-3-4-5-6-7-8-9-10-11-12-13/h12H,2-11H2,1H3
- InChI Key
- HFJRKMMYBMWEAD-UHFFFAOYSA-N
- Formula
- C12H24O
- SMILES
- CCCCCCCCCCCC=O
- Molecular Weight1
- 184.32
- CAS
- 112-54-9
- Other Names
-
- 1-Dodecanal
- 1-Dodecyl aldehyde
- Aldehyde C-12
- Aldehyde C-12, lauric
- C-12 aldehyde, lauric
- Dodecanaldehyde
- Dodecyl aldehyde
- Duodecylic aldehyde
- Lauraldehyde
- Lauric aldehyde
- Laurinaldehyde
- Lauryl aldehyde
- NSC 46128
- n-Dodecanal
- n-Dodecyl aldehyde
- n-Dodecylic aldehyde
- n-Lauraldehyde
- 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 | 0.6750 | ChemSep v8.3 pure component data Compiled value | |
| μ | 2.58 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -51.11 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -374.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 29.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [68.30; 70.20] | kJ/mol |
|
| ΔvapH° | 68.30 ± 0.90 | kJ/mol | NIST |
| ΔvapH° | 70.20 | kJ/mol | NIST |
| IE | 9.61 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.85 | Relay (1.0) Calculated Property | |
| logPoct/wat | 4.106 | Crippen Calculated Property | |
| McVol | 181.510 | ml/mol | McGowan Calculated Property |
| Pc | 1860.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 4.04e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [182.40; 1440.00] |
|
|
| Inp | 1390.10 | NIST | |
| Inp | 1371.40 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1426.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1416.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1421.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1440.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1403.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1413.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1417.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1404.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1367.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1382.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1413.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1404.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1401.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1393.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1406.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1398.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1403.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1398.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1379.00 | NIST | |
| Inp | 1413.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1394.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1390.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1421.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1422.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1417.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1416.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1417.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1420.00 | NIST | |
| Inp | 1423.00 | NIST | |
| Inp | 1423.00 | NIST | |
| Inp | 1430.00 | NIST | |
| Inp | 1432.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1413.00 | NIST | |
| Inp | 1408.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1409.00 | NIST | |
| Inp | 1415.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1419.00 | NIST | |
| Inp | 1399.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | Outlier 182.40 | NIST | |
| Inp | 1389.00 | NIST | |
| Inp | 1402.00 | NIST | |
| Inp | 1384.00 | NIST | |
| Inp | 1386.00 | NIST | |
| Inp | 1405.00 | NIST | |
| Inp | 1414.00 | NIST | |
| Inp | 1407.00 | NIST | |
| Inp | 1396.00 | NIST | |
| Inp | 1387.00 | NIST | |
| Inp | 1392.00 | NIST | |
| Inp | 1391.00 | NIST | |
| Inp | 1385.00 | NIST | |
| Inp | 1388.00 | NIST | |
| Inp | 1383.00 | NIST | |
| Inp | 1412.00 | NIST | |
| Inp | 1395.00 | NIST | |
| Inp | 1411.00 | NIST | |
| Inp | 1421.00 | NIST | |
| Inp | 1410.00 | NIST | |
| Inp | 1418.00 | NIST | |
| Inp | 1432.00 | NIST | |
| Inp | 1397.00 | NIST | |
| Inp | 1375.00 | NIST | |
| Inp | 1390.10 | NIST | |
| Inp | Outlier 182.40 | NIST | |
| Ip | [1673.00; 1738.00] |
|
|
| Ip | 1709.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1715.00 | NIST | |
| Ip | 1729.00 | NIST | |
| Ip | 1729.00 | NIST | |
| Ip | 1718.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1716.00 | NIST | |
| Ip | 1685.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1728.00 | NIST | |
| Ip | 1728.00 | NIST | |
| Ip | 1718.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1698.00 | NIST | |
| Ip | 1711.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1720.00 | NIST | |
| Ip | 1685.00 | NIST | |
| Ip | 1718.00 | NIST | |
| Ip | 1700.00 | NIST | |
| Ip | 1735.00 | NIST | |
| Ip | 1724.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1704.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1696.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1719.00 | NIST | |
| Ip | 1726.00 | NIST | |
| Ip | 1701.00 | NIST | |
| Ip | Outlier 1673.00 | NIST | |
| Ip | 1695.00 | NIST | |
| Ip | 1713.00 | NIST | |
| Ip | 1701.00 | NIST | |
| Ip | 1706.00 | NIST | |
| Ip | 1712.00 | NIST | |
| Ip | 1707.00 | NIST | |
| Ip | 1705.00 | NIST | |
| Ip | 1709.00 | NIST | |
| Ip | 1716.00 | NIST | |
| Ip | 1716.00 | NIST | |
| Ip | 1738.00 | NIST | |
| Ip | 1711.00 | NIST | |
| Ip | 1716.00 | NIST | |
| Ip | 1719.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1698.00 | NIST | |
| Ip | 1682.00 | NIST | |
| Ip | 1699.00 | NIST | |
| Ip | 1713.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1720.00 | NIST | |
| Ip | 1737.00 | NIST | |
| Ip | 1682.00 | NIST | |
| Ip | 1682.00 | NIST | |
| Ip | 1695.00 | NIST | |
| Ip | 1713.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1720.00 | NIST | |
| Ip | 1733.00 | NIST | |
| Ip | 1724.00 | NIST | |
| Ip | 1689.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1732.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1685.00 | NIST | |
| Ip | 1687.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1695.00 | NIST | |
| Ip | 1695.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1697.00 | NIST | |
| Ip | 1709.00 | NIST | |
| Ip | 1710.00 | NIST | |
| Ip | 1722.00 | NIST | |
| Ip | 1728.00 | NIST | |
| Ip | 1708.00 | NIST | |
| Ip | 1735.00 | NIST | |
| Ip | Outlier 1673.00 | NIST | |
| Ip | 1712.00 | NIST | |
| Ip | 1716.00 | NIST | |
| Ip | 1695.00 | NIST | |
| Ip | 1713.00 | NIST | |
| Ip | 1689.00 | NIST | |
| Ip | 1685.00 | NIST | |
| Tboil | [504.15; 523.15] | K |
|
| Tboil | 523.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 511.15 ± 5.00 | K | NIST |
| Tboil | 504.15 ± 5.00 | K | NIST |
| Tc | 685.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [284.00; 319.00] | K |
|
| Tfus | 285.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 285.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 317.00 ± 4.00 | K | NIST |
| Tfus | 284.00 ± 20.00 | K | NIST |
| Tfus | 311.90 ± 3.00 | K | NIST |
| Tfus | 319.00 ± 2.00 | K | NIST |
| Tfus | 316.00 ± 4.00 | K | NIST |
| Tfus | 284.30 ± 20.00 | K | NIST |
| Tfus | 317.70 ± 2.00 | K | NIST |
| Ttriple | 285.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 7.20 | ChemSep v8.3 pure component data Compiled value | |
| URi | 8.64 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.685 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2800000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 56.50 | kJ/mol | 440.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 458.20 | K | 13.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [285.52; 721.50] | 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 | 2.12900e+02 | |||
| Coefficient B | 6.19860e+02 | |||
| Coefficient C | 1.58180e+03 | |||
| Coefficient D | 3.99880e+02 | |||
| Coefficient E | 7.28810e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 285.52 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 380.43 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 459.75 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 524.23 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 576.85 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 619.46 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 653.74 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 681.29 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 703.50 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 721.50 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [386.41; 532.45] | J/mol×K | [298.15; 523.15] |
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 | 1.92900e+02 | |||
| Coefficient B | 6.49040e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 523.15 | |||
| Cp,liquid | 386.41 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 402.64 | J/mol×K | 323.15 | Calculated Property |
| Cp,liquid | 418.86 | J/mol×K | 348.15 | Calculated Property |
| Cp,liquid | 435.09 | J/mol×K | 373.15 | Calculated Property |
| Cp,liquid | 451.32 | J/mol×K | 398.15 | Calculated Property |
| Cp,liquid | 467.54 | J/mol×K | 423.15 | Calculated Property |
| Cp,liquid | 483.77 | J/mol×K | 448.15 | Calculated Property |
| Cp,liquid | 499.99 | J/mol×K | 473.15 | Calculated Property |
| Cp,liquid | 516.22 | J/mol×K | 498.15 | Calculated Property |
| Cp,liquid | 532.45 | J/mol×K | 523.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0022698; 0.0003764] | Pa×s | [285.15; 523.15] |
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 | -1.01100e+01 | |||
| Coefficient B | 1.13010e+03 | |||
| Coefficient C | 1.03960e-02 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 523.15 | |||
| η | 0.0022698 | Pa×s | 285.15 | Calculated Property |
| η | 0.0016230 | Pa×s | 311.59 | Calculated Property |
| η | 0.0012231 | Pa×s | 338.04 | Calculated Property |
| η | 0.0009604 | Pa×s | 364.48 | Calculated Property |
| η | 0.0007793 | Pa×s | 390.93 | Calculated Property |
| η | 0.0006493 | Pa×s | 417.37 | Calculated Property |
| η | 0.0005529 | Pa×s | 443.82 | Calculated Property |
| η | 0.0004794 | Pa×s | 470.26 | Calculated Property |
| η | 0.0004221 | Pa×s | 496.71 | Calculated Property |
| η | 0.0003764 | Pa×s | 523.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [72.20; 0.00] | kJ/mol | [285.15; 685.00] |
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 | 9.09020e+01 | |||
| Coefficient B | 4.27850e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.85000e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 708 K. | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 685.00 | |||
| ΔvapH | 72.20 | kJ/mol | 285.15 | Calculated Property |
| ΔvapH | 68.65 | kJ/mol | 329.58 | Calculated Property |
| ΔvapH | 64.84 | kJ/mol | 374.01 | Calculated Property |
| ΔvapH | 60.70 | kJ/mol | 418.43 | Calculated Property |
| ΔvapH | 56.15 | kJ/mol | 462.86 | Calculated Property |
| ΔvapH | 51.03 | kJ/mol | 507.29 | Calculated Property |
| ΔvapH | 45.12 | kJ/mol | 551.72 | Calculated Property |
| ΔvapH | 37.94 | kJ/mol | 596.14 | Calculated Property |
| ΔvapH | 28.20 | kJ/mol | 640.57 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 685.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [400.22; 536.62] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.68735e+01 | |||
| Coefficient B | -5.20653e+03 | |||
| Coefficient C | -8.63080e+01 | |||
| Temperature range, min. | 400.22 | |||
| Temperature range, max. | 536.62 | |||
| Pvap | 1.33 | kPa | 400.22 | Calculated Property |
| Pvap | 2.86 | kPa | 415.38 | Calculated Property |
| Pvap | 5.74 | kPa | 430.53 | Calculated Property |
| Pvap | 10.87 | kPa | 445.69 | Calculated Property |
| Pvap | 19.53 | kPa | 460.84 | Calculated Property |
| Pvap | 33.54 | kPa | 476.00 | Calculated Property |
| Pvap | 55.31 | kPa | 491.15 | Calculated Property |
| Pvap | 87.98 | kPa | 506.31 | Calculated Property |
| Pvap | 135.48 | kPa | 521.46 | Calculated Property |
| Pvap | 202.65 | kPa | 536.62 | Calculated Property |
| Pvap | [4.04e-04; 2407.67] | kPa | [285.15; 708.00] |
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 | 2.87212e+02 | |||
| Coefficient B | -1.84590e+04 | |||
| Coefficient C | -4.26090e+01 | |||
| Coefficient D | 3.70980e-02 | |||
| Coefficient E | 1.00000e+00 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 708.00 | |||
| Pvap | 4.04e-04 | kPa | 285.15 | Calculated Property |
| Pvap | 0.03 | kPa | 332.13 | Calculated Property |
| Pvap | 0.66 | kPa | 379.12 | Calculated Property |
| Pvap | 5.56 | kPa | 426.10 | Calculated Property |
| Pvap | 27.22 | kPa | 473.08 | Calculated Property |
| Pvap | 93.44 | kPa | 520.07 | Calculated Property |
| Pvap | 253.62 | kPa | 567.05 | Calculated Property |
| Pvap | 588.68 | kPa | 614.03 | Calculated Property |
| Pvap | 1231.57 | kPa | 661.02 | Calculated Property |
| Pvap | 2407.67 | kPa | 708.00 | Calculated Property |
| Pvap | [5.35e-04; 1799.58] | kPa | [285.15; 685.00] |
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 | 1.59818e+02 | |||
| Coefficient B | -1.42801e+04 | |||
| Coefficient C | -2.08974e+01 | |||
| Coefficient D | 1.05969e-05 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 685.00 | |||
| Pvap | 5.35e-04 | kPa | 285.15 | Calculated Property |
| Pvap | 0.03 | kPa | 329.58 | Calculated Property |
| Pvap | 0.50 | kPa | 374.01 | Calculated Property |
| Pvap | 4.05 | kPa | 418.43 | Calculated Property |
| Pvap | 19.69 | kPa | 462.86 | Calculated Property |
| Pvap | 68.26 | kPa | 507.29 | Calculated Property |
| Pvap | 187.59 | kPa | 551.72 | Calculated Property |
| Pvap | 439.29 | kPa | 596.14 | Calculated Property |
| Pvap | 922.13 | kPa | 640.57 | Calculated Property |
| Pvap | 1799.58 | kPa | 685.00 | Calculated Property |
| Pvap | [0.13; 100.07] | kPa | [350.80; 530.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.66763e+01 | |||
| Coefficient B | -6.10515e+03 | |||
| Coefficient C | -2.42060e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 350.80 | |||
| Temperature range, max. | 530.00 | |||
| Pvap | 0.13 | kPa | 350.80 | Calculated Property |
| Pvap | 0.39 | kPa | 370.71 | Calculated Property |
| Pvap | 1.01 | kPa | 390.62 | Calculated Property |
| Pvap | 2.39 | kPa | 410.53 | Calculated Property |
| Pvap | 5.20 | kPa | 430.44 | Calculated Property |
| Pvap | 10.49 | kPa | 450.36 | Calculated Property |
| Pvap | 19.87 | kPa | 470.27 | Calculated Property |
| Pvap | 35.67 | kPa | 490.18 | Calculated Property |
| Pvap | 61.02 | kPa | 510.09 | Calculated Property |
| Pvap | 100.07 | kPa | 530.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [834.45; 269.08] | kg/m3 | [285.15; 708.00] |
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 | 7.03800e+01 | |||
| Coefficient B | 2.61560e-01 | |||
| Coefficient C | 7.08000e+02 | |||
| Coefficient D | 3.29250e-01 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 708.00 | |||
| ρl | 834.45 | kg/m3 | 285.15 | Calculated Property |
| ρl | 799.28 | kg/m3 | 332.13 | Calculated Property |
| ρl | 762.72 | kg/m3 | 379.12 | Calculated Property |
| ρl | 724.39 | kg/m3 | 426.10 | Calculated Property |
| ρl | 683.77 | kg/m3 | 473.08 | Calculated Property |
| ρl | 640.06 | kg/m3 | 520.07 | Calculated Property |
| ρl | 591.85 | kg/m3 | 567.05 | Calculated Property |
| ρl | 536.33 | kg/m3 | 614.03 | Calculated Property |
| ρl | 465.91 | kg/m3 | 661.02 | Calculated Property |
| ρl | 269.08 | kg/m3 | 708.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.10] | W/m×K | [523.15; 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 | -2.35200e+00 | |||
| Coefficient B | 8.55480e-02 | |||
| Coefficient C | -2.70330e+03 | |||
| Coefficient D | -4.08140e+07 | |||
| Temperature range, min. | 523.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 523.15 | Calculated Property |
| λgas | 0.03 | W/m×K | 576.13 | Calculated Property |
| λgas | 0.04 | W/m×K | 629.12 | Calculated Property |
| λgas | 0.05 | W/m×K | 682.10 | Calculated Property |
| λgas | 0.05 | W/m×K | 735.08 | Calculated Property |
| λgas | 0.06 | W/m×K | 788.07 | Calculated Property |
| λgas | 0.07 | W/m×K | 841.05 | Calculated Property |
| λgas | 0.08 | W/m×K | 894.03 | Calculated Property |
| λgas | 0.09 | W/m×K | 947.02 | 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 | [285.15; 523.15] |
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 | 2.01470e-01 | |||
| Coefficient B | -2.07290e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 285.15 | |||
| Temperature range, max. | 523.15 | |||
| λliquid | 0.14 | W/m×K | 285.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 311.59 | Calculated Property |
| λliquid | 0.13 | W/m×K | 338.04 | Calculated Property |
| λliquid | 0.13 | W/m×K | 364.48 | Calculated Property |
| λliquid | 0.12 | W/m×K | 390.93 | Calculated Property |
| λliquid | 0.11 | W/m×K | 417.37 | Calculated Property |
| λliquid | 0.11 | W/m×K | 443.82 | Calculated Property |
| λliquid | 0.10 | W/m×K | 470.26 | Calculated Property |
| λliquid | 0.10 | W/m×K | 496.71 | Calculated Property |
| λliquid | 0.09 | W/m×K | 523.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Dodecanal.
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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