- InChI
- InChI=1S/C10H12/c1-3-9-7-5-6-8-10(9)4-2/h3,5-8H,1,4H2,2H3
- InChI Key
- VTPNYMSKBPZSTF-UHFFFAOYSA-N
- Formula
- C10H12
- SMILES
- C=Cc1ccccc1CC
- Molecular Weight1
- 132.20
- CAS
- 7564-63-8
- Other Names
-
- 1-Ethyl-2-vinylbenzene
- 2-Ethylstyrene
- 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).
- ΔvapH : Enthalpy of vaporization at a given temperature (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).
- 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 | 0.3575 | Relay (1.0) Calculated Property | |
| ΔfG° | 223.94 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 102.78 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 14.03 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 51.32 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.30 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.40 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.892 | Crippen Calculated Property | |
| McVol | 123.700 | ml/mol | McGowan Calculated Property |
| Pc | 3018.96 | kPa | Joback Calculated Property |
| Inp | [1086.40; 1091.00] |
|
|
| Inp | 1091.00 | NIST | |
| Inp | 1086.40 | NIST | |
| Inp | 1091.00 | NIST | |
| Tboil | 458.78 | K | Relay (1.0) Calculated Property |
| Tc | 672.73 | K | Relay (1.0) Calculated Property |
| Tfus | [197.55; 197.65] | K |
|
| Tfus | 197.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 197.55 ± 0.50 | K | NIST |
| Vc | 0.451 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 46.30 | kJ/mol | 388.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [153.10; 385.16] | 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 | -2.87990e+01 | |||
| Coefficient B | 7.95420e-01 | |||
| Coefficient C | -5.07260e-04 | |||
| Coefficient D | 1.25800e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 153.10 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 194.69 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 231.39 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 263.61 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 291.75 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 316.21 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 337.38 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 355.67 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 371.46 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 385.16 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0061923; 0.0002038] | Pa×s | [197.60; 467.16] |
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 | -1.10006e+01 | |||
| Coefficient B | 1.16904e+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. | 197.60 | |||
| Temperature range, max. | 467.16 | |||
| η | 0.0061923 | Pa×s | 197.60 | Calculated Property |
| η | 0.0028422 | Pa×s | 227.55 | Calculated Property |
| η | 0.0015637 | Pa×s | 257.50 | Calculated Property |
| η | 0.0009743 | Pa×s | 287.45 | Calculated Property |
| η | 0.0006638 | Pa×s | 317.41 | Calculated Property |
| η | 0.0004832 | Pa×s | 347.36 | Calculated Property |
| η | 0.0003699 | Pa×s | 377.31 | Calculated Property |
| η | 0.0002945 | Pa×s | 407.26 | Calculated Property |
| η | 0.0002419 | Pa×s | 437.21 | Calculated Property |
| η | 0.0002038 | Pa×s | 467.16 | Calculated Property |
Similar Compounds
Find more compounds similar to o-Ethylvinylbenzene.
Sources
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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