- InChI
- InChI=1S/C11H22/c1-3-5-7-9-11-10-8-6-4-2/h5,7H,3-4,6,8-11H2,1-2H3
- InChI Key
- SDTYFWAQLSIEBH-UHFFFAOYSA-N
- Formula
- C11H22
- SMILES
- CCC=CCCCCCCC
- Molecular Weight1
- 154.29
- CAS
- 60669-40-1
- 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).
- Inp : Non-polar retention indices.
- Tboil : Normal Boiling Point Temperature (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 | 0.4537 | Relay (1.0) Calculated Property | |
| ΔfG° | 121.96 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -186.43 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 24.45 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 54.89 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.85 | eV | Relay (1.0) Calculated Property |
| log10WS | -5.65 | Relay (1.0) 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 | [1005.00; 1005.00] |
|
|
| Inp | 1005.00 | NIST | |
| Inp | 1005.00 | NIST | |
| Tboil | 456.49 | K | Relay (1.0) Calculated Property |
| Tc | 633.88 | K | Relay (1.0) Calculated Property |
| Tfus | 206.85 | K | Relay (1.0) Calculated Property |
| Vc | 0.630 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [224.83; 556.25] | 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 | -2.12930e+01 | |||
| Coefficient B | 1.06884e+00 | |||
| Coefficient C | -6.58400e-04 | |||
| Coefficient D | 1.67100e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 224.83 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 281.83 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 332.56 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 377.53 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 417.29 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 452.35 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 483.25 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 510.51 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 534.67 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 556.25 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0058574; 0.0002131] | Pa×s | [208.65; 437.28] |
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 | -1.14781e+01 | |||
| Coefficient B | 1.32244e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 208.65 | |||
| Temperature range, max. | 437.28 | |||
| η | 0.0058574 | Pa×s | 208.65 | Calculated Property |
| η | 0.0029441 | Pa×s | 234.05 | Calculated Property |
| η | 0.0016932 | Pa×s | 259.46 | Calculated Property |
| η | 0.0010747 | Pa×s | 284.86 | Calculated Property |
| η | 0.0007349 | Pa×s | 310.26 | Calculated Property |
| η | 0.0005323 | Pa×s | 335.67 | Calculated Property |
| η | 0.0004034 | Pa×s | 361.07 | Calculated Property |
| η | 0.0003171 | Pa×s | 386.47 | Calculated Property |
| η | 0.0002568 | Pa×s | 411.88 | Calculated Property |
| η | 0.0002131 | Pa×s | 437.28 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [350.82; 487.04] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.56360e+01 | |||
| Coefficient B | -4.29666e+03 | |||
| Coefficient C | -7.08790e+01 | |||
| Temperature range, min. | 350.82 | |||
| Temperature range, max. | 487.04 | |||
| Pvap | 1.33 | kPa | 350.82 | Calculated Property |
| Pvap | 2.93 | kPa | 365.96 | Calculated Property |
| Pvap | 5.96 | kPa | 381.09 | Calculated Property |
| Pvap | 11.36 | kPa | 396.23 | Calculated Property |
| Pvap | 20.42 | kPa | 411.36 | Calculated Property |
| Pvap | 34.95 | kPa | 426.50 | Calculated Property |
| Pvap | 57.23 | kPa | 441.63 | Calculated Property |
| Pvap | 90.16 | kPa | 456.77 | Calculated Property |
| Pvap | 137.26 | kPa | 471.90 | Calculated Property |
| Pvap | 202.66 | kPa | 487.04 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-Undecene.
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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