- InChI
- InChI=1S/C11H22/c1-3-5-7-9-11-10-8-6-4-2/h3,5H,4,6-11H2,1-2H3/b5-3+
- InChI Key
- JOHIXGUTSXXADV-HWKANZROSA-N
- Formula
- C11H22
- SMILES
- CC=CCCCCCCCC
- Molecular Weight1
- 154.29
- CAS
- 693-61-8
- Other Names
-
- (E)- and (Z)-2-Undecene
- (E)-2-Undecene
- trans-2-Undecene
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- 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).
- Inp : Non-polar retention indices.
- 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 |
|---|---|---|---|
| ΔfG° | 121.96 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -153.15 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 24.45 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 40.04 | kJ/mol | Joback Calculated Property |
| log10WS | -4.28 | Crippen Calculated Property | |
| logPoct/wat | 4.313 | Crippen Calculated Property | |
| McVol | 161.550 | ml/mol | McGowan Calculated Property |
| Pc | 2025.41 | kPa | Joback Calculated Property |
| Inp | [1096.00; 1104.00] |
|
|
| Inp | 1097.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1096.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1097.00 | NIST | |
| Inp | 1102.90 | NIST | |
| Inp | 1101.00 | NIST | |
| Inp | 1104.00 | NIST | |
| Inp | 1099.00 | NIST | |
| Inp | 1102.00 | NIST | |
| Inp | 1097.00 | NIST | |
| I | [1160.00; 1173.00] |
|
|
| I | 1164.00 | NIST | |
| I | 1165.00 | NIST | |
| I | 1166.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1161.00 | NIST | |
| I | 1160.00 | NIST | |
| I | 1163.80 | NIST | |
| I | 1166.50 | NIST | |
| I | 1161.10 | NIST | |
| I | 1163.80 | NIST | |
| I | 1166.50 | NIST | |
| I | 1161.10 | NIST | |
| I | 1163.00 | NIST | |
| I | Outlier 1173.00 | NIST | |
| Tboil | 455.24 | K | Joback Calculated Property |
| Tc | 624.41 | K | Joback Calculated Property |
| Tfus | 208.65 | K | Joback Calculated Property |
| Vc | 0.631 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [344.60; 430.08] | J/mol×K | [455.24; 624.41] |
|
| Cp,gas | 344.60 | J/mol×K | 455.24 | Joback Calculated Property |
| Cp,gas | 360.43 | J/mol×K | 483.44 | Joback Calculated Property |
| Cp,gas | 375.59 | J/mol×K | 511.63 | Joback Calculated Property |
| Cp,gas | 390.12 | J/mol×K | 539.83 | Joback Calculated Property |
| Cp,gas | 404.02 | J/mol×K | 568.02 | Joback Calculated Property |
| Cp,gas | 417.34 | J/mol×K | 596.22 | Joback Calculated Property |
| Cp,gas | 430.08 | J/mol×K | 624.41 | Joback Calculated Property |
| η | [0.0001891; 0.0058574] | Pa×s | [208.65; 455.24] |
|
| η | 0.0058574 | Pa×s | 208.65 | Joback Calculated Property |
| η | 0.0020642 | Pa×s | 249.75 | Joback Calculated Property |
| η | 0.0009768 | Pa×s | 290.85 | Joback Calculated Property |
| η | 0.0005563 | Pa×s | 331.95 | Joback Calculated Property |
| η | 0.0003587 | Pa×s | 373.04 | Joback Calculated Property |
| η | 0.0002523 | Pa×s | 414.14 | Joback Calculated Property |
| η | 0.0001891 | Pa×s | 455.24 | Joback Calculated Property |
| ΔvapH | 53.00 | kJ/mol | 363.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 348.20 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [347.88; 488.73] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45880e+01 | |||
| Coefficient B | -3.71922e+03 | |||
| Coefficient C | -8.78050e+01 | |||
| Temperature range, min. | 347.88 | |||
| Temperature range, max. | 488.73 | |||
| Pvap | 1.33 | kPa | 347.88 | Calculated Property |
| Pvap | 3.00 | kPa | 363.53 | Calculated Property |
| Pvap | 6.19 | kPa | 379.18 | Calculated Property |
| Pvap | 11.87 | kPa | 394.83 | Calculated Property |
| Pvap | 21.37 | kPa | 410.48 | Calculated Property |
| Pvap | 36.42 | kPa | 426.13 | Calculated Property |
| Pvap | 59.21 | kPa | 441.78 | Calculated Property |
| Pvap | 92.38 | kPa | 457.43 | Calculated Property |
| Pvap | 139.02 | kPa | 473.08 | Calculated Property |
| Pvap | 202.64 | kPa | 488.73 | Calculated Property |
Similar Compounds
Find more compounds similar to 2-Undecene, (E)-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.