- InChI
- InChI=1S/C10H12/c1-2-3-7-10-8-5-4-6-9-10/h2-6,8-9H,7H2,1H3
- InChI Key
- VUKHQPGJNTXTPY-UHFFFAOYSA-N
- Formula
- C10H12
- SMILES
- CC=CCc1ccccc1
- Molecular Weight1
- 132.20
- CAS
- 1560-06-1
- Other Names
-
- 1-Phenyl-2-butene
- 1-Phenylbutene-2
- 1-phenylbut-2-ene
- 2-Butene, 1-phenyl-
- 2-butenylbenzene
- 4-Phenyl-2-butene
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- 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).
- 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).
- 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 |
|---|---|---|---|
| ΔcH°liquid | -5672.20 | kJ/mol | NIST |
| ΔfG° | 225.95 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 104.02 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 15.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 40.09 | kJ/mol | Joback Calculated Property |
| log10WS | -2.97 | Crippen Calculated Property | |
| logPoct/wat | 2.805 | Crippen Calculated Property | |
| McVol | 123.700 | ml/mol | McGowan Calculated Property |
| Pc | 3103.64 | kPa | Joback Calculated Property |
| Inp | [186.80; 1064.00] |
|
|
| Inp | 1064.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | 1024.00 | NIST | |
| Inp | 1028.00 | NIST | |
| Inp | Outlier 186.80 | NIST | |
| I | [1414.00; 1487.00] |
|
|
| I | 1487.00 | NIST | |
| I | 1414.00 | NIST | |
| Tboil | [449.15; 449.20] | K |
|
| Tboil | 449.20 | K | NIST |
| Tboil | 449.15 ± 2.00 | K | NIST |
| Tc | 673.98 | K | Joback Calculated Property |
| Tfus | 223.80 | K | Joback Calculated Property |
| Vc | 0.468 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [240.15; 315.65] | J/mol×K | [459.04; 673.98] |
|
| Cp,gas | 240.15 | J/mol×K | 459.04 | Joback Calculated Property |
| Cp,gas | 254.92 | J/mol×K | 494.86 | Joback Calculated Property |
| Cp,gas | 268.75 | J/mol×K | 530.69 | Joback Calculated Property |
| Cp,gas | 281.69 | J/mol×K | 566.51 | Joback Calculated Property |
| Cp,gas | 293.79 | J/mol×K | 602.33 | Joback Calculated Property |
| Cp,gas | 305.09 | J/mol×K | 638.16 | Joback Calculated Property |
| Cp,gas | 315.65 | J/mol×K | 673.98 | Joback Calculated Property |
| η | [0.0001899; 0.0034135] | Pa×s | [223.80; 459.04] |
|
| η | 0.0034135 | Pa×s | 223.80 | Joback Calculated Property |
| η | 0.0014730 | Pa×s | 263.01 | Joback Calculated Property |
| η | 0.0007906 | Pa×s | 302.21 | Joback Calculated Property |
| η | 0.0004895 | Pa×s | 341.42 | Joback Calculated Property |
| η | 0.0003345 | Pa×s | 380.63 | Joback Calculated Property |
| η | 0.0002455 | Pa×s | 419.83 | Joback Calculated Property |
| η | 0.0001899 | Pa×s | 459.04 | Joback Calculated Property |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [331.32; 478.54] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.43653e+01 | |||
| Coefficient B | -3.73490e+03 | |||
| Coefficient C | -6.60140e+01 | |||
| Temperature range, min. | 331.32 | |||
| Temperature range, max. | 478.54 | |||
| Pvap | 1.33 | kPa | 331.32 | Calculated Property |
| Pvap | 3.02 | kPa | 347.68 | Calculated Property |
| Pvap | 6.25 | kPa | 364.04 | Calculated Property |
| Pvap | 12.00 | kPa | 380.39 | Calculated Property |
| Pvap | 21.60 | kPa | 396.75 | Calculated Property |
| Pvap | 36.78 | kPa | 413.11 | Calculated Property |
| Pvap | 59.69 | kPa | 429.47 | Calculated Property |
| Pvap | 92.92 | kPa | 445.82 | Calculated Property |
| Pvap | 139.45 | kPa | 462.18 | Calculated Property |
| Pvap | 202.66 | kPa | 478.54 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 2-butenyl-.
Sources
- Crippen Method
- Crippen Method
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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that the value is more than 2 standard deviations away from the
property mean.