- InChI
- InChI=1S/C11H22O/c1-2-3-4-5-6-7-8-9-10-11-12/h11H,2-10H2,1H3
- InChI Key
- KMPQYAYAQWNLME-UHFFFAOYSA-N
- Formula
- C11H22O
- SMILES
- CCCCCCCCCCC=O
- Molecular Weight1
- 170.29
- CAS
- 112-44-7
- Other Names
-
- 1-Undecanal
- Aldehyde C-11
- Aldehyde C-11, undecylic
- C-11 Aldehyde, undecylic
- Hendecanal
- Hendecanaldehyde
- NSC 22578
- Undecanaldehyde
- Undecyl aldehyde
- Undecylic aldehyde
- n-Undecanal
- n-Undecyl aldehyde
- 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 | 0.6205 | ChemSep v8.3 pure component data Compiled value | |
| μ | 2.58 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -58.96 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -351.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfusH° | 26.54 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [64.60; 69.30] | kJ/mol |
|
| ΔvapH° | 64.60 ± 0.50 | kJ/mol | NIST |
| ΔvapH° | 69.30 | kJ/mol | NIST |
| IE | 9.59 | eV | Relay (1.0) Calculated Property |
| log10WS | -4.36 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.716 | Crippen Calculated Property | |
| McVol | 167.420 | ml/mol | McGowan Calculated Property |
| Pc | 2000.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.41e-04 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [239.08; 1354.00] |
|
|
| Inp | 1278.50 | NIST | |
| Inp | 1263.40 | NIST | |
| Inp | 1273.10 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1317.00 | NIST | |
| Inp | 1317.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1281.90 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1315.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1301.00 | NIST | |
| Inp | 1299.00 | NIST | |
| Inp | 1307.90 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1304.00 | NIST | |
| Inp | 1304.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1308.80 | NIST | |
| Inp | 1320.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1316.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1278.00 | NIST | |
| Inp | 1285.70 | NIST | |
| Inp | 1285.90 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1272.00 | NIST | |
| Inp | 1280.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1309.20 | NIST | |
| Inp | 1314.00 | NIST | |
| Inp | 1295.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1298.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1317.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1320.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1303.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1354.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1284.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1274.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1282.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1281.00 | NIST | |
| Inp | 1291.00 | NIST | |
| Inp | 1301.00 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1304.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1296.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1283.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1294.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1313.00 | NIST | |
| Inp | 1280.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1300.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | 1316.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1314.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1307.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1314.00 | NIST | |
| Inp | 1319.00 | NIST | |
| Inp | 1321.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1326.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1290.00 | NIST | |
| Inp | 1304.00 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1310.60 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1289.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | 1308.00 | NIST | |
| Inp | 1289.00 | NIST | |
| Inp | Outlier 239.10 | NIST | |
| Inp | Outlier 239.08 | NIST | |
| Inp | 1310.00 | NIST | |
| Inp | 1309.00 | NIST | |
| Inp | 1306.00 | NIST | |
| Inp | 1318.00 | NIST | |
| Inp | 1325.00 | NIST | |
| Inp | 1304.00 | NIST | |
| Inp | 1287.00 | NIST | |
| Inp | 1285.00 | NIST | |
| Inp | Outlier 239.10 | NIST | |
| Inp | 1315.00 | NIST | |
| Inp | 1305.00 | NIST | |
| Inp | 1307.90 | NIST | |
| Inp | 1292.00 | NIST | |
| Inp | 1288.00 | NIST | |
| Inp | 1311.00 | NIST | |
| Inp | 1286.00 | NIST | |
| Inp | 1293.00 | NIST | |
| Ip | [1580.00; 1649.00] |
|
|
| Ip | 1609.00 | NIST | |
| Ip | 1609.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1606.00 | NIST | |
| Ip | Outlier 1649.00 | NIST | |
| Ip | 1622.00 | NIST | |
| Ip | 1625.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1587.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1624.00 | NIST | |
| Ip | 1624.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1594.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1630.00 | NIST | |
| Ip | 1618.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1612.00 | NIST | |
| Ip | 1594.70 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1606.00 | NIST | |
| Ip | 1591.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1596.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1611.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1592.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1601.00 | NIST | |
| Ip | 1622.00 | NIST | |
| Ip | 1622.00 | NIST | |
| Ip | 1630.00 | NIST | |
| Ip | 1634.00 | NIST | |
| Ip | 1634.00 | NIST | |
| Ip | 1613.00 | NIST | |
| Ip | 1611.00 | NIST | |
| Ip | 1614.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1597.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1607.00 | NIST | |
| Ip | 1583.00 | NIST | |
| Ip | 1589.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | 1622.00 | NIST | |
| Ip | Outlier 1645.00 | NIST | |
| Ip | 1617.00 | NIST | |
| Ip | 1622.00 | NIST | |
| Ip | 1617.00 | NIST | |
| Ip | 1589.00 | NIST | |
| Ip | 1585.00 | NIST | |
| Ip | 1598.00 | NIST | |
| Ip | 1595.00 | NIST | |
| Ip | 1609.00 | NIST | |
| Ip | 1604.00 | NIST | |
| Ip | 1609.00 | NIST | |
| Ip | 1610.00 | NIST | |
| Ip | 1600.00 | NIST | |
| Ip | 1634.00 | NIST | |
| Ip | 1593.00 | NIST | |
| Ip | 1583.00 | NIST | |
| Ip | 1580.00 | NIST | |
| Ip | 1618.00 | NIST | |
| Ip | 1594.70 | NIST | |
| Ip | 1591.00 | NIST | |
| Ip | 1599.00 | NIST | |
| Ip | 1617.00 | NIST | |
| Ip | 1609.00 | NIST | |
| Tboil | [506.15; 545.15] | K |
|
| Tboil | 506.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 545.15 ± 5.00 | K | NIST |
| Tc | 672.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [269.00; 273.15] | K |
|
| Tfus | 271.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 273.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 269.00 ± 3.00 | K | NIST |
| Ttriple | 273.15 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 6.66 | ChemSep v8.3 pure component data Compiled value | |
| URi | 7.97 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.632 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2740000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 60.20 | kJ/mol | 344.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [383.00; 390.20] | K | [0.70; 2.40] |
|
| Tboilr | 385.20 | K | 0.70 | NIST |
| Tboilr | 383.00 | K | 0.70 | NIST |
| Tboilr | 390.20 | K | 2.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [262.76; 664.61] | 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 | 1.97240e+02 | |||
| Coefficient B | 5.75460e+02 | |||
| Coefficient C | 1.62180e+03 | |||
| Coefficient D | 3.75690e+02 | |||
| Coefficient E | 7.38150e+02 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 262.76 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 349.77 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 421.91 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 480.48 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 528.69 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 568.18 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 600.28 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 626.29 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 647.40 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 664.61 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [357.66; 481.79] | J/mol×K | [298.15; 506.15] |
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 | 1.79740e+02 | |||
| Coefficient B | 5.96760e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 506.15 | |||
| Cp,liquid | 357.66 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 371.46 | J/mol×K | 321.26 | Calculated Property |
| Cp,liquid | 385.25 | J/mol×K | 344.37 | Calculated Property |
| Cp,liquid | 399.04 | J/mol×K | 367.48 | Calculated Property |
| Cp,liquid | 412.83 | J/mol×K | 390.59 | Calculated Property |
| Cp,liquid | 426.62 | J/mol×K | 413.71 | Calculated Property |
| Cp,liquid | 440.41 | J/mol×K | 436.82 | Calculated Property |
| Cp,liquid | 454.21 | J/mol×K | 459.93 | Calculated Property |
| Cp,liquid | 468.00 | J/mol×K | 483.04 | Calculated Property |
| Cp,liquid | 481.79 | J/mol×K | 506.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0024376; 0.0003672] | Pa×s | [273.15; 506.15] |
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 | -1.02100e+01 | |||
| Coefficient B | 1.12750e+03 | |||
| Coefficient C | 1.16730e-02 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 506.15 | |||
| η | 0.0024376 | Pa×s | 273.15 | Calculated Property |
| η | 0.0017070 | Pa×s | 299.04 | Calculated Property |
| η | 0.0012652 | Pa×s | 324.93 | Calculated Property |
| η | 0.0009803 | Pa×s | 350.82 | Calculated Property |
| η | 0.0007867 | Pa×s | 376.71 | Calculated Property |
| η | 0.0006494 | Pa×s | 402.59 | Calculated Property |
| η | 0.0005487 | Pa×s | 428.48 | Calculated Property |
| η | 0.0004727 | Pa×s | 454.37 | Calculated Property |
| η | 0.0004138 | Pa×s | 480.26 | Calculated Property |
| η | 0.0003672 | Pa×s | 506.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [68.05; 0.00] | kJ/mol | [273.15; 672.00] |
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 | 8.48180e+01 | |||
| Coefficient B | 4.22240e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 6.72000e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 692 K. | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 672.00 | |||
| ΔvapH | 68.05 | kJ/mol | 273.15 | Calculated Property |
| ΔvapH | 64.75 | kJ/mol | 317.47 | Calculated Property |
| ΔvapH | 61.20 | kJ/mol | 361.78 | Calculated Property |
| ΔvapH | 57.34 | kJ/mol | 406.10 | Calculated Property |
| ΔvapH | 53.09 | kJ/mol | 450.42 | Calculated Property |
| ΔvapH | 48.32 | kJ/mol | 494.73 | Calculated Property |
| ΔvapH | 42.79 | kJ/mol | 539.05 | Calculated Property |
| ΔvapH | 36.06 | kJ/mol | 583.37 | Calculated Property |
| ΔvapH | 26.91 | kJ/mol | 627.68 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 672.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [379.42; 533.04] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.51338e+01 | |||
| Coefficient B | -4.45893e+03 | |||
| Coefficient C | -7.90800e+01 | |||
| Temperature range, min. | 379.42 | |||
| Temperature range, max. | 533.04 | |||
| Pvap | 1.33 | kPa | 379.42 | Calculated Property |
| Pvap | 2.96 | kPa | 396.49 | Calculated Property |
| Pvap | 6.07 | kPa | 413.56 | Calculated Property |
| Pvap | 11.59 | kPa | 430.63 | Calculated Property |
| Pvap | 20.85 | kPa | 447.70 | Calculated Property |
| Pvap | 35.61 | kPa | 464.76 | Calculated Property |
| Pvap | 58.13 | kPa | 481.83 | Calculated Property |
| Pvap | 91.18 | kPa | 498.90 | Calculated Property |
| Pvap | 138.08 | kPa | 515.97 | Calculated Property |
| Pvap | 202.66 | kPa | 533.04 | Calculated Property |
| Pvap | [1.41e-04; 2507.98] | kPa | [273.15; 692.00] |
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 | 2.72602e+02 | |||
| Coefficient B | -1.95570e+04 | |||
| Coefficient C | -3.76860e+01 | |||
| Coefficient D | 2.07520e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 692.00 | |||
| Pvap | 1.41e-04 | kPa | 273.15 | Calculated Property |
| Pvap | 0.02 | kPa | 319.69 | Calculated Property |
| Pvap | 0.62 | kPa | 366.23 | Calculated Property |
| Pvap | 5.93 | kPa | 412.77 | Calculated Property |
| Pvap | 29.85 | kPa | 459.31 | Calculated Property |
| Pvap | 100.33 | kPa | 505.84 | Calculated Property |
| Pvap | 262.68 | kPa | 552.38 | Calculated Property |
| Pvap | 593.22 | kPa | 598.92 | Calculated Property |
| Pvap | 1238.40 | kPa | 645.46 | Calculated Property |
| Pvap | 2507.98 | kPa | 692.00 | Calculated Property |
| Pvap | [5.36e-04; 1942.17] | kPa | [273.15; 672.00] |
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 | 1.33696e+02 | |||
| Coefficient B | -1.25365e+04 | |||
| Coefficient C | -1.71082e+01 | |||
| Coefficient D | 8.65866e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 672.00 | |||
| Pvap | 5.36e-04 | kPa | 273.15 | Calculated Property |
| Pvap | 0.03 | kPa | 317.47 | Calculated Property |
| Pvap | 0.54 | kPa | 361.78 | Calculated Property |
| Pvap | 4.44 | kPa | 406.10 | Calculated Property |
| Pvap | 21.87 | kPa | 450.42 | Calculated Property |
| Pvap | 76.36 | kPa | 494.73 | Calculated Property |
| Pvap | 210.14 | kPa | 539.05 | Calculated Property |
| Pvap | 489.57 | kPa | 583.37 | Calculated Property |
| Pvap | 1015.21 | kPa | 627.68 | Calculated Property |
| Pvap | 1942.17 | kPa | 672.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [841.80; 269.45] | kg/m3 | [273.15; 692.00] |
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 | 7.06882e+01 | |||
| Coefficient B | 2.62340e-01 | |||
| Coefficient C | 6.92000e+02 | |||
| Coefficient D | 3.20620e-01 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 692.00 | |||
| ρl | 841.80 | kg/m3 | 273.15 | Calculated Property |
| ρl | 807.01 | kg/m3 | 319.69 | Calculated Property |
| ρl | 770.75 | kg/m3 | 366.23 | Calculated Property |
| ρl | 732.66 | kg/m3 | 412.77 | Calculated Property |
| ρl | 692.21 | kg/m3 | 459.31 | Calculated Property |
| ρl | 648.55 | kg/m3 | 505.84 | Calculated Property |
| ρl | 600.25 | kg/m3 | 552.38 | Calculated Property |
| ρl | 544.41 | kg/m3 | 598.92 | Calculated Property |
| ρl | 473.22 | kg/m3 | 645.46 | Calculated Property |
| ρl | 269.45 | kg/m3 | 692.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.02; 0.10] | W/m×K | [506.15; 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 | -3.09460e+00 | |||
| Coefficient B | 6.94540e-02 | |||
| Coefficient C | -2.16810e+03 | |||
| Coefficient D | -4.81040e+07 | |||
| Temperature range, min. | 506.15 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.02 | W/m×K | 506.15 | Calculated Property |
| λgas | 0.03 | W/m×K | 561.02 | Calculated Property |
| λgas | 0.04 | W/m×K | 615.89 | Calculated Property |
| λgas | 0.04 | W/m×K | 670.77 | Calculated Property |
| λgas | 0.05 | W/m×K | 725.64 | Calculated Property |
| λgas | 0.06 | W/m×K | 780.51 | Calculated Property |
| λgas | 0.07 | W/m×K | 835.38 | Calculated Property |
| λgas | 0.08 | W/m×K | 890.26 | Calculated Property |
| λgas | 0.09 | W/m×K | 945.13 | Calculated Property |
| λgas | 0.10 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.10] | W/m×K | [273.15; 506.15] |
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 | 2.03790e-01 | |||
| Coefficient B | -2.13740e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.15 | |||
| Temperature range, max. | 506.15 | |||
| λliquid | 0.15 | W/m×K | 273.15 | Calculated Property |
| λliquid | 0.14 | W/m×K | 299.04 | Calculated Property |
| λliquid | 0.13 | W/m×K | 324.93 | Calculated Property |
| λliquid | 0.13 | W/m×K | 350.82 | Calculated Property |
| λliquid | 0.12 | W/m×K | 376.71 | Calculated Property |
| λliquid | 0.12 | W/m×K | 402.59 | Calculated Property |
| λliquid | 0.11 | W/m×K | 428.48 | Calculated Property |
| λliquid | 0.11 | W/m×K | 454.37 | Calculated Property |
| λliquid | 0.10 | W/m×K | 480.26 | Calculated Property |
| λliquid | 0.10 | W/m×K | 506.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Undecanal.
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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