- InChI
- InChI=1S/C9H10/c1-3-9-6-4-8(2)5-7-9/h3-7H,1H2,2H3
- InChI Key
- JLBJTVDPSNHSKJ-UHFFFAOYSA-N
- Formula
- C9H10
- SMILES
- C=Cc1ccc(C)cc1
- Molecular Weight1
- 118.18
- CAS
- 622-97-9
- Other Names
-
- 1-Ethenyl-4-methylbenzene
- 1-Methyl-4-ethenylbenzene
- 1-Methyl-4-vinylbenzene
- 1-p-Tolylethene
- 4-Methylstyrene
- 4-Vinyltoluene
- Styrene, p-methyl-
- p-Methyl-styrene
- p-Methylstyrene
- p-Vinyltoluene
- para-Methylstyrene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (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).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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).
- n0 : Refractive Index.
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2830; 0.3250] |
|
|
| ω | 0.2830 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3128 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.3250 | KDB | |
| PAff | 861.70 | kJ/mol | NIST |
| BasG | 832.80 | kJ/mol | NIST |
| ΔfG° | 215.52 | kJ/mol | Joback Calculated Property |
| Δc,grossH | 5042.56 | kJ/mol | KDB |
| Δc,netH | 4822.897 | kJ/mol | KDB |
| ΔfH°gas | 133.16 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 11.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 46.52 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [8.10; 8.20] | eV |
|
| IE | 8.10 ± 0.10 | eV | NIST |
| IE | 8.20 | eV | NIST |
| log10WS | -3.03 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.638 | Crippen Calculated Property | |
| McVol | 109.610 | ml/mol | McGowan Calculated Property |
| Pc | [3303.20; 3543.91] | kPa |
|
| Pc | 3303.20 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3543.91 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 3370.00 | kPa | KDB |
| Inp | [155.70; 1000.00] |
|
|
| Inp | 982.00 | NIST | |
| Inp | 979.00 | NIST | |
| Inp | 980.50 | NIST | |
| Inp | 965.90 | NIST | |
| Inp | 1000.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 978.60 | NIST | |
| Inp | 980.30 | NIST | |
| Inp | 978.60 | NIST | |
| Inp | 980.30 | NIST | |
| Inp | 977.50 | NIST | |
| Inp | 977.60 | NIST | |
| Inp | 977.90 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 966.00 | NIST | |
| Inp | 980.00 | NIST | |
| Inp | 978.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | Outlier 155.70 | NIST | |
| Inp | Outlier 158.68 | NIST | |
| Inp | 982.00 | NIST | |
| Inp | 985.00 | NIST | |
| Inp | 977.50 | NIST | |
| Inp | Outlier 155.70 | NIST | |
| Inp | 966.00 | NIST | |
| Ip | [1348.60; 1396.80] |
|
|
| Ip | 1385.20 | NIST | |
| Ip | 1396.80 | NIST | |
| Ip | 1348.60 | NIST | |
| Ip | 1349.00 | NIST | |
| Ip | 1349.00 | NIST | |
| Tboil | [442.20; 446.00] | K |
|
| Tboil | 442.20 | K | KDB |
| Tboil | 446.00 | K | NIST |
| Tboil | 444.95 ± 2.00 | K | NIST |
| Tboil | 444.65 ± 3.00 | K | NIST |
| Tboil | 445.65 ± 4.00 | K | NIST |
| Tc | [659.70; 675.93] | K |
|
| Tc | 669.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 675.93 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 659.70 | K | KDB |
| Tfus | [202.85; 239.30] | K |
|
| Tfus | 239.10 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 239.00 | K | KDB |
| Tfus | 239.30 ± 0.40 | K | NIST |
| Tfus | 239.00 ± 0.15 | K | NIST |
| Tfus | 235.35 ± 0.50 | K | NIST |
| Tfus | Outlier 202.85 | K | NIST |
| Vc | [0.402; 0.412] | m3/kmol |
|
| Vc | 0.402 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.412 | m3/kmol | KDB |
| Zc | 0.2534370 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [35.98; 47.60] | kJ/mol | [347.00; 442.20] |
|
| ΔvapH | 47.60 | kJ/mol | 347.00 | NIST |
| ΔvapH | 35.98 | kJ/mol | 442.20 | KDB |
| n0 | 1.53950 | 298.15 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [131.89; 333.57] | 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 | -2.78900e+01 | |||
| Coefficient B | 7.00420e-01 | |||
| Coefficient C | -4.52860e-04 | |||
| Coefficient D | 1.13900e-07 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 131.89 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 168.27 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 200.31 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 228.38 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 252.84 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 274.05 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 292.37 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 308.15 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 321.77 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 333.57 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0016547; 0.0001812] | Pa×s | [238.35; 467.75] |
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 | -1.09138e+01 | |||
| Coefficient B | 1.07488e+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. | 238.35 | |||
| Temperature range, max. | 467.75 | |||
| η | 0.0016547 | Pa×s | 238.35 | Calculated Property |
| η | 0.0010703 | Pa×s | 263.84 | Calculated Property |
| η | 0.0007476 | Pa×s | 289.33 | Calculated Property |
| η | 0.0005534 | Pa×s | 314.82 | Calculated Property |
| η | 0.0004285 | Pa×s | 340.30 | Calculated Property |
| η | 0.0003439 | Pa×s | 365.79 | Calculated Property |
| η | 0.0002839 | Pa×s | 391.28 | Calculated Property |
| η | 0.0002400 | Pa×s | 416.77 | Calculated Property |
| η | 0.0002069 | Pa×s | 442.26 | Calculated Property |
| η | 0.0001812 | Pa×s | 467.75 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [326.31; 475.86] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43047e+01 | |||
| Coefficient B | -3.75249e+03 | |||
| Coefficient C | -5.86000e+01 | |||
| Temperature range, min. | 326.31 | |||
| Temperature range, max. | 475.86 | |||
| Pvap | 1.33 | kPa | 326.31 | Calculated Property |
| Pvap | 3.02 | kPa | 342.93 | Calculated Property |
| Pvap | 6.27 | kPa | 359.54 | Calculated Property |
| Pvap | 12.04 | kPa | 376.16 | Calculated Property |
| Pvap | 21.66 | kPa | 392.78 | Calculated Property |
| Pvap | 36.87 | kPa | 409.39 | Calculated Property |
| Pvap | 59.82 | kPa | 426.01 | Calculated Property |
| Pvap | 93.06 | kPa | 442.63 | Calculated Property |
| Pvap | 139.56 | kPa | 459.24 | Calculated Property |
| Pvap | 202.65 | kPa | 475.86 | Calculated Property |
| Pvap | [1.51e-03; 3359.14] | kPa | [239.02; 665.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.42136e+01 | |||
| Coefficient B | -8.61409e+03 | |||
| Coefficient C | -1.00306e+01 | |||
| Coefficient D | 4.65024e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 239.02 | |||
| Temperature range, max. | 665.00 | |||
| Pvap | 1.51e-03 | kPa | 239.02 | Calculated Property |
| Pvap | 0.11 | kPa | 286.35 | Calculated Property |
| Pvap | 1.89 | kPa | 333.68 | Calculated Property |
| Pvap | 14.44 | kPa | 381.01 | Calculated Property |
| Pvap | 64.82 | kPa | 428.34 | Calculated Property |
| Pvap | 204.45 | kPa | 475.68 | Calculated Property |
| Pvap | 506.48 | kPa | 523.01 | Calculated Property |
| Pvap | 1059.93 | kPa | 570.34 | Calculated Property |
| Pvap | 1968.68 | kPa | 617.67 | Calculated Property |
| Pvap | 3359.14 | kPa | 665.00 | Calculated Property |
| Pvap | [0.38; 9.45] | kPa | [304.97; 370.08] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42146e+01 | |||
| Coefficient B | -3.67219e+03 | |||
| Coefficient C | -6.32550e+01 | |||
| Reference | Clements, Wise, et al., 1953 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 304.97 | |||
| Temperature range, max. | 370.08 | |||
| Pvap | 0.38 | kPa | 304.97 | Calculated Property |
| Pvap | 0.58 | kPa | 312.20 | Calculated Property |
| Pvap | 0.89 | kPa | 319.44 | Calculated Property |
| Pvap | 1.32 | kPa | 326.67 | Calculated Property |
| Pvap | 1.91 | kPa | 333.91 | Calculated Property |
| Pvap | 2.72 | kPa | 341.14 | Calculated Property |
| Pvap | 3.80 | kPa | 348.38 | Calculated Property |
| Pvap | 5.23 | kPa | 355.61 | Calculated Property |
| Pvap | 7.08 | kPa | 362.85 | Calculated Property |
| Pvap | 9.45 | kPa | 370.08 | Calculated Property |
| Pvap | [2.73; 98.53] | kPa | [341.80; 443.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40661e+01 | |||
| Coefficient B | -3.49367e+03 | |||
| Coefficient C | -7.43040e+01 | |||
| Reference | Buck, Coles, et al., 1949 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 341.80 | |||
| Temperature range, max. | 443.00 | |||
| Pvap | 2.73 | kPa | 341.80 | Calculated Property |
| Pvap | 4.63 | kPa | 353.04 | Calculated Property |
| Pvap | 7.53 | kPa | 364.29 | Calculated Property |
| Pvap | 11.80 | kPa | 375.53 | Calculated Property |
| Pvap | 17.91 | kPa | 386.78 | Calculated Property |
| Pvap | 26.41 | kPa | 398.02 | Calculated Property |
| Pvap | 37.94 | kPa | 409.27 | Calculated Property |
| Pvap | 53.24 | kPa | 420.51 | Calculated Property |
| Pvap | 73.13 | kPa | 431.76 | Calculated Property |
| Pvap | 98.53 | kPa | 443.00 | Calculated Property |
| Pvap | [0.38; 9.45] | kPa | [304.97; 370.08] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42146e+01 | |||
| Coefficient B | -3.67219e+03 | |||
| Coefficient C | -6.32550e+01 | |||
| Reference | Clements, Wise, et al., 1953, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 304.97 | |||
| Temperature range, max. | 370.08 | |||
| Pvap | 0.38 | kPa | 304.97 | Calculated Property |
| Pvap | 0.58 | kPa | 312.20 | Calculated Property |
| Pvap | 0.89 | kPa | 319.44 | Calculated Property |
| Pvap | 1.32 | kPa | 326.67 | Calculated Property |
| Pvap | 1.91 | kPa | 333.91 | Calculated Property |
| Pvap | 2.72 | kPa | 341.14 | Calculated Property |
| Pvap | 3.80 | kPa | 348.38 | Calculated Property |
| Pvap | 5.23 | kPa | 355.61 | Calculated Property |
| Pvap | 7.08 | kPa | 362.85 | Calculated Property |
| Pvap | 9.45 | kPa | 370.08 | Calculated Property |
| Pvap | [2.73; 98.53] | kPa | [341.80; 443.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40661e+01 | |||
| Coefficient B | -3.49367e+03 | |||
| Coefficient C | -7.43040e+01 | |||
| Reference | Buck, Coles, et al., 1949, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 341.80 | |||
| Temperature range, max. | 443.00 | |||
| Pvap | 2.73 | kPa | 341.80 | Calculated Property |
| Pvap | 4.63 | kPa | 353.04 | Calculated Property |
| Pvap | 7.53 | kPa | 364.29 | Calculated Property |
| Pvap | 11.80 | kPa | 375.53 | Calculated Property |
| Pvap | 17.91 | kPa | 386.78 | Calculated Property |
| Pvap | 26.41 | kPa | 398.02 | Calculated Property |
| Pvap | 37.94 | kPa | 409.27 | Calculated Property |
| Pvap | 53.24 | kPa | 420.51 | Calculated Property |
| Pvap | 73.13 | kPa | 431.76 | Calculated Property |
| Pvap | 98.53 | kPa | 443.00 | Calculated Property |
Similar Compounds
![Tricyclo[8.2.2.2(4,7)]hexadeca-2,4,6,8,10,12,13,15-octaene.](data:image/png;base64,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)
Find more compounds similar to Benzene, 1-ethenyl-4-methyl-.
Sources
- KDB Vapor Pressure Data
- 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).
- Passut and Danner (1973), critical constants and acentric factors ChEDL chemicals 1.5.2, from Passut, C. A.; Danner, R. P. Acentric Factor. A Valuable Correlating Parameter for the Properties of Hydrocarbons. Ind. Eng. Chem. Process Des. Dev. 1973, 12, 365-368.
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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