- InChI
- InChI=1S/C14H28/c1-3-5-7-9-11-13-14-12-10-8-6-4-2/h5,7H,3-4,6,8-14H2,1-2H3
- InChI Key
- QKTFNIWYLYTNIS-UHFFFAOYSA-N
- Formula
- C14H28
- SMILES
- CCC=CCCCCCCCCCC
- Molecular Weight1
- 196.37
- CAS
- 41446-67-7
- 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 | 0.5771 | Relay (1.0) Calculated Property | |
| ΔfG° | 147.22 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -252.17 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 32.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 69.35 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.89 | eV | Relay (1.0) Calculated Property |
| log10WS | -6.58 | Relay (1.0) Calculated Property | |
| logPoct/wat | 5.483 | Crippen Calculated Property | |
| McVol | 203.820 | ml/mol | McGowan Calculated Property |
| Pc | 1587.28 | kPa | Joback Calculated Property |
| Inp | [1382.00; 1416.00] |
|
|
| Inp | 1382.00 | NIST | |
| Inp | 1416.00 | NIST | |
| Tboil | 510.97 | K | Relay (1.0) Calculated Property |
| Tc | 684.99 | K | Relay (1.0) Calculated Property |
| Tfus | 240.74 | K | Relay (1.0) Calculated Property |
| Vc | 0.800 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [288.47; 711.02] | 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 | -2.40200e+01 | |||
| Coefficient B | 1.35384e+00 | |||
| Coefficient C | -8.21600e-04 | |||
| Coefficient D | 2.02800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 288.47 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 361.09 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 425.79 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 483.22 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 534.02 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 578.84 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 618.30 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 653.06 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 683.75 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 711.02 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0054364; 0.0002011] | Pa×s | [242.46; 483.06] |
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 | -1.18340e+01 | |||
| Coefficient B | 1.60492e+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. | 242.46 | |||
| Temperature range, max. | 483.06 | |||
| η | 0.0054364 | Pa×s | 242.46 | Calculated Property |
| η | 0.0028173 | Pa×s | 269.19 | Calculated Property |
| η | 0.0016441 | Pa×s | 295.93 | Calculated Property |
| η | 0.0010490 | Pa×s | 322.66 | Calculated Property |
| η | 0.0007170 | Pa×s | 349.39 | Calculated Property |
| η | 0.0005173 | Pa×s | 376.13 | Calculated Property |
| η | 0.0003897 | Pa×s | 402.86 | Calculated Property |
| η | 0.0003041 | Pa×s | 429.59 | Calculated Property |
| η | 0.0002444 | Pa×s | 456.32 | Calculated Property |
| η | 0.0002011 | Pa×s | 483.06 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [402.52; 542.81] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.65756e+01 | |||
| Coefficient B | -5.12329e+03 | |||
| Coefficient C | -8.79760e+01 | |||
| Temperature range, min. | 402.52 | |||
| Temperature range, max. | 542.81 | |||
| Pvap | 1.33 | kPa | 402.52 | Calculated Property |
| Pvap | 2.88 | kPa | 418.11 | Calculated Property |
| Pvap | 5.79 | kPa | 433.70 | Calculated Property |
| Pvap | 10.98 | kPa | 449.28 | Calculated Property |
| Pvap | 19.73 | kPa | 464.87 | Calculated Property |
| Pvap | 33.85 | kPa | 480.46 | Calculated Property |
| Pvap | 55.74 | kPa | 496.05 | Calculated Property |
| Pvap | 88.46 | kPa | 511.63 | Calculated Property |
| Pvap | 135.88 | kPa | 527.22 | Calculated Property |
| Pvap | 202.65 | kPa | 542.81 | Calculated Property |
Similar Compounds
Find more compounds similar to 3-Tetradecene.
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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