- InChI
- InChI=1S/C10H10/c1-3-9-6-5-7-10(4-2)8-9/h3-8H,1-2H2
- InChI Key
- PRJNEUBECVAVAG-UHFFFAOYSA-N
- Formula
- C10H10
- SMILES
- C=Cc1cccc(C=C)c1
- Molecular Weight1
- 130.19
- CAS
- 108-57-6
- Other Names
-
- 1,3-Diethenylbenzene
- 1,3-Divinylbenzene
- Benzene, m-divinyl-
- Divinylbenzene
- m-Divinylbenzene
- m-Vinylstyrene
- 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).
- 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).
- Tboilr : Boiling point at reduced pressure (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 |
|---|---|---|---|
| ΔfG° | 311.78 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 226.19 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 12.75 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 39.45 | kJ/mol | Joback Calculated Property |
| log10WS | -3.12 | Crippen Calculated Property | |
| logPoct/wat | 2.973 | Crippen Calculated Property | |
| McVol | 119.400 | ml/mol | McGowan Calculated Property |
| Pc | 3163.27 | kPa | Joback Calculated Property |
| Inp | [184.20; 1108.00] |
|
|
| Inp | 1091.30 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1092.00 | NIST | |
| Inp | 1084.80 | NIST | |
| Inp | 1085.20 | NIST | |
| Inp | 1086.00 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | Outlier 184.20 | NIST | |
| Inp | 1091.00 | NIST | |
| Inp | Outlier 184.20 | NIST | |
| Inp | 1091.30 | NIST | |
| Inp | 1086.00 | NIST | |
| I | [1541.00; 1541.00] |
|
|
| I | 1541.00 | NIST | |
| I | 1541.00 | NIST | |
| I | 1541.00 | NIST | |
| Tboil | 453.22 | K | Joback Calculated Property |
| Tc | 668.56 | K | Joback Calculated Property |
| Tfus | 220.90 ± 0.05 | K | NIST |
| Vc | 0.450 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [224.07; 292.44] | J/mol×K | [453.22; 668.56] |
|
| Cp,gas | 224.07 | J/mol×K | 453.22 | Joback Calculated Property |
| Cp,gas | 237.39 | J/mol×K | 489.11 | Joback Calculated Property |
| Cp,gas | 249.89 | J/mol×K | 525.00 | Joback Calculated Property |
| Cp,gas | 261.61 | J/mol×K | 560.89 | Joback Calculated Property |
| Cp,gas | 272.58 | J/mol×K | 596.78 | Joback Calculated Property |
| Cp,gas | 282.84 | J/mol×K | 632.67 | Joback Calculated Property |
| Cp,gas | 292.44 | J/mol×K | 668.56 | Joback Calculated Property |
| η | [0.0002153; 0.0019528] | Pa×s | [237.88; 453.22] |
|
| η | 0.0019528 | Pa×s | 237.88 | Joback Calculated Property |
| η | 0.0010628 | Pa×s | 273.77 | Joback Calculated Property |
| η | 0.0006660 | Pa×s | 309.66 | Joback Calculated Property |
| η | 0.0004599 | Pa×s | 345.55 | Joback Calculated Property |
| η | 0.0003405 | Pa×s | 381.44 | Joback Calculated Property |
| η | 0.0002655 | Pa×s | 417.33 | Joback Calculated Property |
| η | 0.0002153 | Pa×s | 453.22 | Joback Calculated Property |
| ΔvapH | 48.30 | kJ/mol | 379.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 325.20 | K | 0.40 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [344.89; 472.91] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.69595e+01 | |||
| Coefficient B | -4.94851e+03 | |||
| Coefficient C | -4.80710e+01 | |||
| Temperature range, min. | 344.89 | |||
| Temperature range, max. | 472.91 | |||
| Pvap | 1.33 | kPa | 344.89 | Calculated Property |
| Pvap | 2.86 | kPa | 359.11 | Calculated Property |
| Pvap | 5.73 | kPa | 373.34 | Calculated Property |
| Pvap | 10.84 | kPa | 387.56 | Calculated Property |
| Pvap | 19.48 | kPa | 401.79 | Calculated Property |
| Pvap | 33.46 | kPa | 416.01 | Calculated Property |
| Pvap | 55.20 | kPa | 430.24 | Calculated Property |
| Pvap | 87.85 | kPa | 444.46 | Calculated Property |
| Pvap | 135.37 | kPa | 458.69 | Calculated Property |
| Pvap | 202.66 | kPa | 472.91 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,3-diethenyl-.
Mixtures
Sources
- Crippen Method
- Crippen Method
- Diffusion coefficients of 2-fluoroanisole, 2-bromoanisole, allylbenzene and 1,3-divinylbenzene at infinite dilution in supercritical carbon dioxide
- Joback Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.