- InChI
- InChI=1S/C11H14/c1-2-3-5-8-11-9-6-4-7-10-11/h2,4,6-7,9-10H,1,3,5,8H2
- InChI Key
- RURREWSZSUQSNB-UHFFFAOYSA-N
- Formula
- C11H14
- SMILES
- C=CCCCc1ccccc1
- Molecular Weight1
- 146.23
- CAS
- 1075-74-7
- Other Names
-
- 1-Pentene, 5-phenyl-
- 1-Phenyl-4-pentene
- 4-Pentenylbenzene
- 5-Phenyl-1-pentene
- 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 | 0.3802 | Relay (1.0) Calculated Property | |
| ΔfG° | 241.99 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 100.90 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 17.01 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 53.93 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.74 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.74 | Relay (1.0) Calculated Property | |
| logPoct/wat | 3.195 | Crippen Calculated Property | |
| McVol | 137.790 | ml/mol | McGowan Calculated Property |
| Pc | 2767.17 | kPa | Joback Calculated Property |
| Inp | [1140.00; 1140.00] |
|
|
| Inp | 1140.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Tboil | 471.15 ± 2.00 | K | NIST |
| Tc | 686.07 | K | Relay (1.0) Calculated Property |
| Tfus | 200.13 | K | Relay (1.0) Calculated Property |
| Vc | 0.506 | m3/kmol | Relay (1.0) Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [171.77; 439.79] | 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 | -4.40070e+01 | |||
| Coefficient B | 9.49900e-01 | |||
| Coefficient C | -6.28700e-04 | |||
| Coefficient D | 1.62600e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 171.77 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 220.56 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 263.40 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 300.80 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 333.27 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 361.34 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 385.51 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 406.30 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 424.22 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 439.79 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0034173; 0.0002170] | Pa×s | [238.39; 476.76] |
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 | -1.11928e+01 | |||
| Coefficient B | 1.31446e+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. | 238.39 | |||
| Temperature range, max. | 476.76 | |||
| η | 0.0034173 | Pa×s | 238.39 | Calculated Property |
| η | 0.0019690 | Pa×s | 264.88 | Calculated Property |
| η | 0.0012541 | Pa×s | 291.36 | Calculated Property |
| η | 0.0008611 | Pa×s | 317.85 | Calculated Property |
| η | 0.0006265 | Pa×s | 344.33 | Calculated Property |
| η | 0.0004770 | Pa×s | 370.82 | Calculated Property |
| η | 0.0003766 | Pa×s | 397.31 | Calculated Property |
| η | 0.0003062 | Pa×s | 423.79 | Calculated Property |
| η | 0.0002552 | Pa×s | 450.28 | Calculated Property |
| η | 0.0002170 | Pa×s | 476.76 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [351.32; 500.62] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46783e+01 | |||
| Coefficient B | -4.00574e+03 | |||
| Coefficient C | -7.29640e+01 | |||
| Temperature range, min. | 351.32 | |||
| Temperature range, max. | 500.62 | |||
| Pvap | 1.33 | kPa | 351.32 | Calculated Property |
| Pvap | 3.00 | kPa | 367.91 | Calculated Property |
| Pvap | 6.17 | kPa | 384.50 | Calculated Property |
| Pvap | 11.83 | kPa | 401.09 | Calculated Property |
| Pvap | 21.28 | kPa | 417.68 | Calculated Property |
| Pvap | 36.28 | kPa | 434.26 | Calculated Property |
| Pvap | 59.03 | kPa | 450.85 | Calculated Property |
| Pvap | 92.18 | kPa | 467.44 | Calculated Property |
| Pvap | 138.87 | kPa | 484.03 | Calculated Property |
| Pvap | 202.67 | kPa | 500.62 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 4-pentenyl-.
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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