- InChI
- InChI=1S/C8H8/c1-2-8-6-4-3-5-7-8/h2-7H,1H2
- InChI Key
- PPBRXRYQALVLMV-UHFFFAOYSA-N
- Formula
- C8H8
- SMILES
- C=Cc1ccccc1
- Molecular Weight1
- 104.15
- CAS
- 100-42-5
- Other Names
-
- Annamene
- Benzene, vinyl-
- Bulstren K-525-19
- Cinnamene
- Cinnamenol
- Cinnaminol
- Cinnamol
- Ethylene, phenyl-
- NCI-C02200
- NSC 62785
- Phenethylene
- Stirolo
- Styreen
- Styren
- Styrene monomer
- Styrol
- Styrol (German)
- Styrole
- Styrolene
- Styropol SO
- Vinylbenzen
- Vinylbenzene (styrene)
- Vinylbenzol
- benzene, ethenyl-
- ethenylbenzene
- ethenylbenzene (styrene)
- phenylethene
- phenylethylene
- vinylbenzene
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2570 | KDB | |
| PAff | 839.50 | kJ/mol | NIST |
| Tig | 763.15 | K | KDB |
| BasG | 809.20 | kJ/mol | NIST |
| ΔcH°liquid | [-4438.35; -4336.70] | kJ/mol |
|
| ΔcH°liquid | -4395.63 ± 0.59 | kJ/mol | NIST |
| ΔcH°liquid | -4394.87 ± 0.84 | kJ/mol | NIST |
| ΔcH°liquid | -4438.35 ± 0.92 | kJ/mol | NIST |
| ΔcH°liquid | -4379.80 ± 6.30 | kJ/mol | NIST |
| ΔcH°liquid | -4399.50 | kJ/mol | NIST |
| ΔcH°liquid | -4374.40 | kJ/mol | NIST |
| ΔcH°liquid | -4379.00 | kJ/mol | NIST |
| ΔcH°liquid | -4431.30 | kJ/mol | NIST |
| ΔcH°liquid | -4336.70 | kJ/mol | NIST |
| μ | 0.10 | debye | KDB |
| LFL | 1.10 | % in Air | KDB |
| UFL | 6.10 | % in Air | KDB |
| Tflash,cc | 307.04 | K | KDB |
| Tflash,oc | 304.26 | K | KDB |
| ΔfG° | 213.90 | kJ/mol | KDB |
| Rg | 3.8000 | KDB | |
| Δc,grossH | 4395.33 | kJ/mol | KDB |
| Δc,netH | 4219.313 | kJ/mol | KDB |
| ΔfH°gas | [-147.50; 151.50] | kJ/mol |
|
| ΔfH°gas | -147.50 | kJ/mol | KDB |
| ΔfH°gas | 146.90 ± 1.00 | kJ/mol | NIST |
| ΔfH°gas | 151.50 | kJ/mol | NIST |
| ΔfH°gas | 131.50 ± 4.00 | kJ/mol | NIST |
| ΔfH°gas | -15.10 | kJ/mol | NIST |
| ΔfH°liquid | [-58.60; 108.00] | kJ/mol |
|
| ΔfH°liquid | 103.40 ± 0.92 | kJ/mol | NIST |
| ΔfH°liquid | 108.00 | kJ/mol | NIST |
| ΔfH°liquid | 87.60 ± 4.00 | kJ/mol | NIST |
| ΔfH°liquid | -58.60 | kJ/mol | NIST |
| ΔfusH° | 9.24 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [43.20; 43.93] | kJ/mol |
|
| ΔvapH° | 43.93 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 43.90 | kJ/mol | NIST |
| ΔvapH° | 43.50 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 43.50 | kJ/mol | NIST |
| ΔvapH° | 43.20 | kJ/mol | NIST |
| ΔvapH° | 43.93 ± 0.42 | kJ/mol | NIST |
| ΔvapH° | 43.90 | kJ/mol | NIST |
| ΔvapH° | 43.50 ± 0.40 | kJ/mol | NIST |
| IE | [8.20; 8.58] | eV |
|
| IE | 8.46 ± 0.00 | eV | NIST |
| IE | 8.46 ± 0.00 | eV | NIST |
| IE | 8.47 | eV | NIST |
| IE | 8.43 | eV | NIST |
| IE | Outlier 8.20 ± 0.10 | eV | NIST |
| IE | 8.42 | eV | NIST |
| IE | 8.40 ± 0.02 | eV | NIST |
| IE | 8.28 ± 0.04 | eV | NIST |
| IE | 8.53 | eV | NIST |
| IE | 8.43 ± 0.01 | eV | NIST |
| IE | 8.42 | eV | NIST |
| IE | 8.47 ± 0.02 | eV | NIST |
| IE | 8.48 | eV | NIST |
| IE | 8.58 | eV | NIST |
| IE | 8.50 | eV | NIST |
| IE | 8.49 | eV | NIST |
| IE | 8.55 | eV | NIST |
| IE | 8.55 | eV | NIST |
| log10WS | [-2.82; -2.70] |
|
|
| log10WS | -2.70 | Aq. Solubility Prediction | |
| log10WS | -2.82 | Estimated Solubility | |
| logPoct/wat | 2.330 | Crippen Calculated Property | |
| McVol | 95.520 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 2 | KDB | |
| Pc | 3990.00 | kPa | KDB |
| Inp | [125.20; 916.00] |
|
|
| Inp | 874.35 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 890.50 | NIST | |
| Inp | 874.50 | NIST | |
| Inp | 874.40 | NIST | |
| Inp | 874.90 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 874.35 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 877.80 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 874.50 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 890.50 | NIST | |
| Inp | 897.30 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 860.90 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 874.50 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 916.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 874.40 | NIST | |
| Inp | 874.70 | NIST | |
| Inp | 874.90 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 915.00 | NIST | |
| Inp | 914.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 895.20 | NIST | |
| Inp | 907.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 880.30 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 892.60 | NIST | |
| Inp | 888.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 898.00 | NIST | |
| Inp | 894.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 900.02 | NIST | |
| Inp | 905.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 885.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 882.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 884.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 891.40 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 870.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 873.29 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 872.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 877.00 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 874.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 866.00 | NIST | |
| Inp | 869.00 | NIST | |
| Inp | 896.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 911.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 867.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 889.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 897.00 | NIST | |
| Inp | 910.00 | NIST | |
| Inp | 881.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 893.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 903.00 | NIST | |
| Inp | 883.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 904.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 887.00 | NIST | |
| Inp | 890.00 | NIST | |
| Inp | 862.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 868.00 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | 876.00 | NIST | |
| Inp | 880.00 | NIST | |
| Inp | 886.00 | NIST | |
| Inp | 879.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | 900.00 | NIST | |
| Inp | 871.00 | NIST | |
| Inp | Outlier 125.30 | NIST | |
| Inp | Outlier 125.20 | NIST | |
| Inp | Outlier 146.81 | NIST | |
| Inp | Outlier 135.50 | NIST | |
| Inp | Outlier 135.00 | NIST | |
| Inp | Outlier 127.70 | NIST | |
| Inp | Outlier 135.40 | NIST | |
| Inp | Outlier 127.70 | NIST | |
| Inp | 875.00 | NIST | |
| Inp | Outlier 125.30 | NIST | |
| Inp | 873.00 | NIST | |
| Inp | 863.00 | NIST | |
| Inp | 878.00 | NIST | |
| Inp | 895.00 | NIST | |
| Inp | 891.00 | NIST | |
| Inp | 892.00 | NIST | |
| Inp | 883.00 | NIST | |
| I | [1228.70; 1310.00] |
|
|
| I | 1229.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1243.00 | NIST | |
| I | Outlier 1291.70 | NIST | |
| I | Outlier 1300.00 | NIST | |
| I | 1255.10 | NIST | |
| I | 1283.80 | NIST | |
| I | 1281.90 | NIST | |
| I | 1282.60 | NIST | |
| I | 1284.80 | NIST | |
| I | Outlier 1293.50 | NIST | |
| I | Outlier 1295.00 | NIST | |
| I | 1228.70 | NIST | |
| I | 1275.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1260.00 | NIST | |
| I | 1251.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1244.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1259.00 | NIST | |
| I | 1256.00 | NIST | |
| I | 1265.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1230.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1261.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1236.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1269.00 | NIST | |
| I | 1275.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1229.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1247.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1268.00 | NIST | |
| I | 1277.00 | NIST | |
| I | 1270.00 | NIST | |
| I | 1239.00 | NIST | |
| I | 1249.00 | NIST | |
| I | 1257.00 | NIST | |
| I | 1248.00 | NIST | |
| I | 1250.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1273.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1240.00 | NIST | |
| I | 1242.00 | NIST | |
| I | 1243.00 | NIST | |
| I | 1252.00 | NIST | |
| I | 1253.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1248.00 | NIST | |
| I | Outlier 1310.00 | NIST | |
| I | 1254.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1274.00 | NIST | |
| I | 1255.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1262.00 | NIST | |
| I | 1272.00 | NIST | |
| I | 1241.00 | NIST | |
| I | 1267.00 | NIST | |
| I | 1245.00 | NIST | |
| I | 1285.00 | NIST | |
| I | 1264.00 | NIST | |
| I | 1263.00 | NIST | |
| I | 1266.00 | NIST | |
| I | 1262.00 | NIST | |
| S°gas | 345.10 ± 2.10 | J/mol×K | NIST |
| S°liquid | [237.57; 240.50] | J/mol×K |
|
| S°liquid | 240.50 | J/mol×K | NIST |
| S°liquid | 237.57 | J/mol×K | NIST |
| S°liquid | 237.60 | J/mol×K | NIST |
| S°liquid | 237.57 | J/mol×K | NIST |
| Tboil | [413.15; 420.65] | K |
|
| Tboil | 418.30 | K | KDB |
| Tboil | 418.40 | K | NIST |
| Tboil | 418.35 | K | NIST |
| Tboil | 420.65 ± 5.00 | K | NIST |
| Tboil | 417.65 ± 5.00 | K | NIST |
| Tboil | 418.25 ± 1.50 | K | NIST |
| Tboil | 418.75 ± 0.30 | K | NIST |
| Tboil | 418.15 ± 1.00 | K | NIST |
| Tboil | 418.65 ± 2.00 | K | NIST |
| Tboil | 418.29 ± 0.20 | K | NIST |
| Tboil | 418.45 ± 0.20 | K | NIST |
| Tboil | 418.45 ± 0.30 | K | NIST |
| Tboil | 418.65 ± 1.00 | K | NIST |
| Tboil | 418.95 ± 0.30 | K | NIST |
| Tboil | 419.15 ± 1.50 | K | NIST |
| Tboil | 418.35 ± 0.30 | K | NIST |
| Tboil | 418.25 ± 0.30 | K | NIST |
| Tboil | 419.00 ± 0.50 | K | NIST |
| Tboil | 419.00 ± 0.50 | K | NIST |
| Tboil | 416.00 ± 4.00 | K | NIST |
| Tboil | Outlier 413.15 ± 2.00 | K | NIST |
| Tc | 647.00 | K | KDB |
| Tfus | [197.55; 242.55] | K |
|
| Tfus | 242.50 | K | KDB |
| Tfus | 242.55 | K | NIST |
| Tfus | 242.38 ± 0.40 | K | NIST |
| Tfus | 242.47 ± 0.15 | K | NIST |
| Tfus | 242.47 ± 0.20 | K | NIST |
| Tfus | 242.50 ± 0.20 | K | NIST |
| Tfus | 242.50 ± 0.20 | K | NIST |
| Tfus | Outlier 197.55 ± 0.05 | K | NIST |
| Tfus | 228.15 ± 5.00 | K | NIST |
| Tfus | 242.25 ± 0.50 | K | NIST |
| Tfus | 242.55 ± 0.20 | K | NIST |
| Tfus | 239.85 ± 0.40 | K | NIST |
| Ttriple | [242.47; 242.47] | K |
|
| Ttriple | 242.47 ± 0.07 | K | NIST |
| Ttriple | 242.47 ± 0.10 | K | NIST |
| Ttriple | 242.47 ± 0.10 | K | NIST |
| Ttriple | 242.47 ± 0.07 | K | NIST |
| Vc | 0.352 | m3/kmol | Relay (1.0) Calculated Property |
| Zra | 0.26 | KDB |
Temperature Dependent Properties
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [305.95; 447.65] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.39212e+01 | |||
| Coefficient B | -3.31078e+03 | |||
| Coefficient C | -6.31110e+01 | |||
| Temperature range, min. | 305.95 | |||
| Temperature range, max. | 447.65 | |||
| Pvap | 1.33 | kPa | 305.95 | Calculated Property |
| Pvap | 3.06 | kPa | 321.69 | Calculated Property |
| Pvap | 6.38 | kPa | 337.44 | Calculated Property |
| Pvap | 12.27 | kPa | 353.18 | Calculated Property |
| Pvap | 22.09 | kPa | 368.93 | Calculated Property |
| Pvap | 37.53 | kPa | 384.67 | Calculated Property |
| Pvap | 60.69 | kPa | 400.42 | Calculated Property |
| Pvap | 94.02 | kPa | 416.16 | Calculated Property |
| Pvap | 140.31 | kPa | 431.91 | Calculated Property |
| Pvap | 202.64 | kPa | 447.65 | Calculated Property |
| Pvap | [0.01; 4030.19] | kPa | [242.54; 648.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.60058e+01 | |||
| Coefficient B | -8.11907e+03 | |||
| Coefficient C | -1.04313e+01 | |||
| Coefficient D | 5.61169e-06 | |||
| Temperature range, min. | 242.54 | |||
| Temperature range, max. | 648.00 | |||
| Pvap | 0.01 | kPa | 242.54 | Calculated Property |
| Pvap | 0.44 | kPa | 287.59 | Calculated Property |
| Pvap | 5.17 | kPa | 332.64 | Calculated Property |
| Pvap | 30.25 | kPa | 377.69 | Calculated Property |
| Pvap | 112.99 | kPa | 422.74 | Calculated Property |
| Pvap | 312.86 | kPa | 467.80 | Calculated Property |
| Pvap | 705.72 | kPa | 512.85 | Calculated Property |
| Pvap | 1380.25 | kPa | 557.90 | Calculated Property |
| Pvap | 2442.56 | kPa | 602.95 | Calculated Property |
| Pvap | 4030.19 | kPa | 648.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Styrene.
Mixtures
- Benzene, nitro- + Styrene
- Nitrogen + Styrene
- Styrene + Oxygen
- Nitrogen + Styrene + Oxygen
- 1,3-Dioxolan-2-one, 4-methyl- + Styrene
- Styrene + Cyclohexanone
- Styrene + Dimethyl Sulfoxide
- Styrene + Ethyl Acetate
- Benzene + Styrene
- Styrene + Formamide, N,N-dimethyl- + Ethyl Acetate
- Benzene + Styrene + Formamide, N,N-dimethyl-
- Styrene + Carbon dioxide
- Styrene + Carbonic acid, dimethyl ester
- Styrene + 1-Butanol, 3-methyl-, acetate
- Styrene + Carbon dioxide + Benzene, ethyl-
- Styrene + Carbon dioxide + Safrole
- Styrene + Water
- Styrene + Benzene, ethyl-
- Styrene + Thiophene, tetrahydro-, 1,1-dioxide
- Styrene + Benzene, ethyl- + Thiophene, tetrahydro-, 1,1-dioxide
Find more mixtures with Styrene.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Volumetric Properties of 3-Methylbutyl Ethanoate with Ethyl Acrylate, Butyl Acrylate, Methyl Methacrylate, and Styrene at 25 C
- Volumetric, Viscometric, Ultrasonic, and Refractive Index Properties of Liquid Mixtures of Benzene with Industrially Important Monomers at Different Temperatures
- Solubility of chlorobutane, ethyl methacrylate and trifluoroethyl acrylate in supercritical carbon dioxide
- Binary and ternary vapor-liquid equilibrium data of the system ethylbenzene + styrene + 3-methyl-N-butylpyridinium tetracyanoborate at vacuum conditions and liquid-liquid equilibrium data of their binary systems
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Gas solubilities of nitrogen or oxygen in benzene, divinylbenzene, styrene and of an equimolar (N2:O2) mixture in styrene at (293-313) K
- Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
- Experimental densities and excess volumes for binary mixtures of (dimethyl sulfoxide + an aromatic hydrocarbon) at temperatures from (293.15 to 353.15) K at atmospheric pressure
- A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
- The volumetric properties of (1,2-propanediol carbonate + benzene, or toluene, or styrene) binary mixtures at temperatures from T = 293.15 K to T = 353.15 K
- Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
- Density, excess volume, and excess coefficient of thermal expansion of the binary systems of dimethyl carbonate with butyl methacrylate, allyl methacrylate, styrene, and vinyl acetate at T = (293.15, 303.15, and 313.15) K
- Binary and ternary LLE data of the system (ethylbenzene + styrene + 1-ethyl-3-methylimidazolium thiocyanate) and binary VLE data of the system (styrene + 1-ethyl-3-methylimidazolium thiocyanate)
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Liquid-liquid extraction of styrene from ethylbenzene using ionic liquids
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Vapour-liquid phase boundaries including the near critical regions of the (CO2 + styrene, CO2 + 1,4-dioxane, and CO2 + N,N-dimethylformamide) systems
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Solubilities of Diethyl Phthalate, Dicyclopentadiene, and Styrene in Ionic Liquid 1-Ethyl-3-methylimidazolium Acetate
- Measurement and Correlation of the Solubilities of Sulfur S8 in 10 Solvents
- Phase Behaviors, Density, and Isothermal Compressibility of Styrene + CO2, Ethylbenzene + CO2, and Ethylbezene + Styrene + CO2 Systems
- Densities and Viscosities of Binary Mixtures of Ethylbenzene + N-Methyl-2-pyrrolidone, Ethylbenzene + Sulfolane, and Styrene + Octane from (303.15 to 353.15) K and Atmospheric Pressure
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Styrene
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
- Binary and Ternary Vapor-Liquid Equilibrium Data of the System (Ethylbenzene + Styrene + 4-Methyl-N-butylpyridinium Tetrafluoroborate) at Vacuum Conditions and Liquid-Liquid Equilibrium Data of Their Binary Systems
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Phase Equilibria of the Systems CO2 + Styrene, CO2 + Safrole, and CO2 + Styrene + Safrole
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Limiting Binary Diffusivities of Aniline, Styrene, and Mesitylene in Supercritical Carbon Dioxide
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
- Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
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