- InChI
- InChI=1S/C11H22O/c1-2-3-4-5-6-7-8-9-10-11-12/h2,12H,1,3-11H2
- InChI Key
- GIEMHYCMBGELGY-UHFFFAOYSA-N
- Formula
- C11H22O
- SMILES
- C=CCCCCCCCCCO
- Molecular Weight1
- 170.30
- CAS
- 112-43-6
- Other Names
-
- 1-Undecen-11-ol
- 10-Undecene-1-ol
- 10-Undecenol
- 10-Undecylen-1-ol
- 11-Hydroxy-1-undecene
- Undec-10-enol
- Undecylenic alcohol
- Undecylenyl alcohol
- undec-10-en-1-ol
- «omega»-Undecenyl alcohol
- «omega»-Undecylenyl 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).
- ΔvapH° : Enthalpy of vaporization at standard conditions (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).
- 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).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7762 | Relay (1.0) Calculated Property | |
| ΔfG° | -7.24 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -317.50 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 27.05 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 87.19 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 9.56 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.68 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.286 | Crippen Calculated Property | |
| McVol | 167.420 | ml/mol | McGowan Calculated Property |
| Pc | 2183.60 | kPa | Joback Calculated Property |
| I | 1664.00 | NIST | |
| Tboil | 525.99 | K | Relay (1.0) Calculated Property |
| Tc | 717.31 | K | Relay (1.0) Calculated Property |
| Tfus | 282.99 | K | Relay (1.0) Calculated Property |
| Vc | 0.625 | m3/kmol | Relay (1.0) Calculated Property |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [405.00; 405.70] | K | [2.00; 2.00] |
|
| Tboilr | 405.00 | K | 2.00 | NIST |
| Tboilr | 405.70 | K | 2.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [241.53; 576.99] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | -4.81100e+00 | |||
| Coefficient B | 1.06280e+00 | |||
| Coefficient C | -6.27900e-04 | |||
| Coefficient D | 1.46900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 241.53 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 299.10 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 350.52 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 396.24 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 436.73 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 472.46 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 503.88 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 531.47 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 555.68 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 576.99 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0248802; 0.0001888] | Pa×s | [272.79; 490.42] |
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 | -1.46935e+01 | |||
| Coefficient B | 3.00063e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 272.79 | |||
| Temperature range, max. | 490.42 | |||
| η | 0.0248802 | Pa×s | 272.79 | Calculated Property |
| η | 0.0101595 | Pa×s | 296.97 | Calculated Property |
| η | 0.0047475 | Pa×s | 321.15 | Calculated Property |
| η | 0.0024679 | Pa×s | 345.33 | Calculated Property |
| η | 0.0013976 | Pa×s | 369.51 | Calculated Property |
| η | 0.0008487 | Pa×s | 393.70 | Calculated Property |
| η | 0.0005460 | Pa×s | 417.88 | Calculated Property |
| η | 0.0003687 | Pa×s | 442.06 | Calculated Property |
| η | 0.0002593 | Pa×s | 466.24 | Calculated Property |
| η | 0.0001888 | Pa×s | 490.42 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [399.32; 572.60] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44069e+01 | |||
| Coefficient B | -4.42933e+03 | |||
| Coefficient C | -8.56130e+01 | |||
| Temperature range, min. | 399.32 | |||
| Temperature range, max. | 572.60 | |||
| Pvap | 1.33 | kPa | 399.32 | Calculated Property |
| Pvap | 3.02 | kPa | 418.57 | Calculated Property |
| Pvap | 6.24 | kPa | 437.83 | Calculated Property |
| Pvap | 11.98 | kPa | 457.08 | Calculated Property |
| Pvap | 21.55 | kPa | 476.33 | Calculated Property |
| Pvap | 36.71 | kPa | 495.59 | Calculated Property |
| Pvap | 59.60 | kPa | 514.84 | Calculated Property |
| Pvap | 92.81 | kPa | 534.09 | Calculated Property |
| Pvap | 139.37 | kPa | 553.35 | Calculated Property |
| Pvap | 202.66 | kPa | 572.60 | Calculated Property |
Similar Compounds
Find more compounds similar to 10-Undecen-1-ol.
Sources
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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