- InChI
- InChI=1S/C8H7Cl/c1-2-7-5-3-4-6-8(7)9/h2-6H,1H2
- InChI Key
- ISRGONDNXBCDBM-UHFFFAOYSA-N
- Formula
- C8H7Cl
- SMILES
- C=Cc1ccccc1Cl
- Molecular Weight1
- 138.59
- CAS
- 2039-87-4
- Other Names
-
- 1-Chloro-2-vinylbenzene
- Benzene, 1-chloro-2-ethenyl-
- Styrene, o-chloro-
- o-Chlorostyrene
- 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).
- Pvap : Vapor pressure (kPa).
- 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 |
|---|---|---|---|
| ω | 0.2937 | Relay (1.0) Calculated Property | |
| ΔfG° | 195.17 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | 118.89 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 13.04 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 47.72 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.60 | eV | Relay (1.0) Calculated Property |
| log10WS | -2.88 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.983 | Crippen Calculated Property | |
| McVol | 107.760 | ml/mol | McGowan Calculated Property |
| Pc | 3607.21 | kPa | Joback Calculated Property |
| Tboil | 461.90 | K | NIST |
| Tc | 691.76 | K | Relay (1.0) Calculated Property |
| Tfus | 210.10 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.390 | m3/kmol | Relay (1.0) Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 46.00 | kJ/mol | 443.00 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | [332.20; 337.80] | K | [0.90; 1.30] |
|
| Tboilr | 332.20 | K | 0.90 | NIST |
| Tboilr | 337.80 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [124.08; 290.25] | 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 | -1.40900e+01 | |||
| Coefficient B | 6.12200e-01 | |||
| Coefficient C | -4.18860e-04 | |||
| Coefficient D | 1.11000e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 124.08 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 154.98 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 181.96 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 205.35 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 225.52 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 242.81 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 257.58 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 270.18 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 280.95 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 290.25 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0046722; 0.0002250] | Pa×s | [210.10; 470.24] |
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 | -1.08494e+01 | |||
| Coefficient B | 1.15204e+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. | 210.10 | |||
| Temperature range, max. | 470.24 | |||
| η | 0.0046722 | Pa×s | 210.10 | Calculated Property |
| η | 0.0024072 | Pa×s | 239.00 | Calculated Property |
| η | 0.0014311 | Pa×s | 267.91 | Calculated Property |
| η | 0.0009415 | Pa×s | 296.81 | Calculated Property |
| η | 0.0006671 | Pa×s | 325.72 | Calculated Property |
| η | 0.0005001 | Pa×s | 354.62 | Calculated Property |
| η | 0.0003915 | Pa×s | 383.53 | Calculated Property |
| η | 0.0003171 | Pa×s | 412.43 | Calculated Property |
| η | 0.0002641 | Pa×s | 441.34 | Calculated Property |
| η | 0.0002250 | Pa×s | 470.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [336.84; 492.68] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46526e+01 | |||
| Coefficient B | -4.16255e+03 | |||
| Coefficient C | -4.70680e+01 | |||
| Temperature range, min. | 336.84 | |||
| Temperature range, max. | 492.68 | |||
| Pvap | 1.33 | kPa | 336.84 | Calculated Property |
| Pvap | 3.00 | kPa | 354.16 | Calculated Property |
| Pvap | 6.18 | kPa | 371.47 | Calculated Property |
| Pvap | 11.84 | kPa | 388.79 | Calculated Property |
| Pvap | 21.30 | kPa | 406.10 | Calculated Property |
| Pvap | 36.32 | kPa | 423.42 | Calculated Property |
| Pvap | 59.08 | kPa | 440.73 | Calculated Property |
| Pvap | 92.23 | kPa | 458.05 | Calculated Property |
| Pvap | 138.90 | kPa | 475.36 | Calculated Property |
| Pvap | 202.64 | kPa | 492.68 | Calculated Property |
Similar Compounds
![2-[2-Chlorophenyl]propenoic acid.](data:image/png;base64,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)
Find more compounds similar to 2-Chlorostyrene.
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
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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