Chemical Properties of Ethylbenzene (CAS 100-41-4)

Ethylbenzene

InChI
InChI=1S/C8H10/c1-2-8-6-4-3-5-7-8/h3-7H,2H2,1H3
InChI Key
YNQLUTRBYVCPMQ-UHFFFAOYSA-N
Formula
C8H10
SMILES
CCc1ccccc1
Molecular Weight1
106.17
CAS
100-41-4
Other Names
  • .alpha.-methyltoluene
  • Aethylbenzol
  • Benzene, ethyl-
  • EB
  • Ethylbenzeen
  • Ethylbenzol
  • Etilbenzene
  • Etylobenzen
  • NCI-C56393
  • NSC 406903
  • Phenylethane
  • UN 1175
  • «alpha»-Methyltoluene
  • «alpha»-Methyltoluene
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Contents

  1. Physical Properties
  2. Temperature Dependent Properties
  3. Pressure Dependent Properties
  4. Datasets
  5. Correlations
  6. Similar Compounds
  7. Mixtures
  8. Sources

Physical Properties

Property Value Unit Source
ω 0.3020 KDB
PAff [788.00; 789.90] kJ/mol Show Hide
PAff 788.00 kJ/mol NIST
PAff 789.90 kJ/mol NIST
Tig 733.15 K KDB
BasG [760.20; 760.30] kJ/mol Show Hide
BasG 760.30 kJ/mol NIST
BasG 760.20 kJ/mol NIST
Cp,liquid 185.44 J/mol×K Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ 0.40 debye KDB
LFL 1.00 % in Air KDB
UFL 6.70 % in Air KDB
Tflash,cc 299.82 K KDB
Tflash,oc 288.15 K KDB
Δf 130.70 kJ/mol KDB
Rg 3.8210 KDB
Δc,grossH 4564.87 kJ/mol KDB
Δc,netH 4344.792 kJ/mol KDB
Δfgas [29.80; 69.30] kJ/mol Show Hide
Δfgas 29.81 kJ/mol KDB
Δfgas 29.80 ± 0.84 kJ/mol NIST
Δfgas 49.00 ± 4.00 kJ/mol NIST
Δfgas 69.30 kJ/mol NIST
Δfliquid [-12.50; 27.00] kJ/mol Show Hide
Δfliquid -12.50 ± 0.84 kJ/mol NIST
Δfliquid 6.80 ± 4.00 kJ/mol NIST
Δfliquid 27.00 kJ/mol NIST
Δfus 10.52 kJ/mol Joback Calculated Property
Δvap 43.45 kJ/mol Relay (1.0) Calculated Property
IE [8.61; 9.38] eV Show Hide
IE 8.77 ± 0.01 eV NIST
IE 8.77 eV NIST
IE 8.61 eV NIST
IE 8.65 ± 0.10 eV NIST
IE 8.76 eV NIST
IE 8.77 ± 0.01 eV NIST
IE 8.75 ± 0.05 eV NIST
IE 8.76 ± 0.01 eV NIST
IE 8.77 ± 0.01 eV NIST
IE 8.77 eV NIST
IE 8.73 eV NIST
IE Outlier 9.38 eV NIST
log10WS [-2.77; -2.77]   Show Hide
log10WS -2.77 Aq. Solubility Prediction
log10WS -2.77 Estimated Solubility
logPoct/wat 2.249 Crippen Calculated Property
McVol 99.820 ml/mol McGowan Calculated Property
NFPA Fire 3 KDB
NFPA Health 2 KDB
Pc 3609.00 kPa KDB
ρc [283.46; 284.52] kg/m3 Show Hide
ρc 284.52 ± 1.06 kg/m3 NIST
ρc 283.46 ± 4.25 kg/m3 NIST
Inp [118.30; 893.00]   Show Hide
Inp 850.60 NIST
Inp 844.50 NIST
Inp 846.80 NIST
Inp 843.40 NIST
Inp 841.80 NIST
Inp 843.50 NIST
Inp 848.10 NIST
Inp 866.85 NIST
Inp 879.95 NIST
Inp 847.30 NIST
Inp 875.40 NIST
Inp 848.34 NIST
Inp 848.34 NIST
Inp 859.20 NIST
Inp 861.00 NIST
Inp 847.00 NIST
Inp 850.00 NIST
Inp 848.00 NIST
Inp 854.80 NIST
Inp 871.10 NIST
Inp 880.00 NIST
Inp 847.80 NIST
Inp 848.10 NIST
Inp 848.10 NIST
Inp 848.20 NIST
Inp 847.60 NIST
Inp 849.00 NIST
Inp 874.00 NIST
Inp 848.00 NIST
Inp 848.00 NIST
Inp 859.00 NIST
Inp 859.00 NIST
Inp 848.00 NIST
Inp 875.00 NIST
Inp 858.40 NIST
Inp 863.30 NIST
Inp 857.30 NIST
Inp 857.00 NIST
Inp 844.60 NIST
Inp 849.70 NIST
Inp 834.60 NIST
Inp 839.80 NIST
Inp 858.00 NIST
Inp 840.00 NIST
Inp 859.00 NIST
Inp 860.00 NIST
Inp 832.80 NIST
Inp 838.50 NIST
Inp 857.00 NIST
Inp 858.00 NIST
Inp 859.00 NIST
Inp 849.00 NIST
Inp 833.30 NIST
Inp 870.00 NIST
Inp 857.00 NIST
Inp 859.00 NIST
Inp 857.00 NIST
Inp 860.00 NIST
Inp 854.00 NIST
Inp 848.00 NIST
Inp 845.00 NIST
Inp 847.80 NIST
Inp 848.20 NIST
Inp 851.40 NIST
Inp 859.00 NIST
Inp 867.00 NIST
Inp 854.00 NIST
Inp 859.00 NIST
Inp 864.00 NIST
Inp 870.00 NIST
Inp 821.00 NIST
Inp 845.30 NIST
Inp 847.70 NIST
Inp 858.90 NIST
Inp 864.20 NIST
Inp 870.10 NIST
Inp 846.00 NIST
Inp 834.10 NIST
Inp 839.50 NIST
Inp 844.60 NIST
Inp 844.60 NIST
Inp 844.80 NIST
Inp 845.30 NIST
Inp 839.40 NIST
Inp 840.60 NIST
Inp 839.00 NIST
Inp 839.20 NIST
Inp 845.30 NIST
Inp 847.70 NIST
Inp 850.00 NIST
Inp 844.00 NIST
Inp 844.00 NIST
Inp 855.20 NIST
Inp 837.00 NIST
Inp 839.00 NIST
Inp 841.56 NIST
Inp 864.00 NIST
Inp 866.00 NIST
Inp 870.00 NIST
Inp 873.00 NIST
Inp 868.00 NIST
Inp 872.00 NIST
Inp 875.00 NIST
Inp 877.00 NIST
Inp 880.00 NIST
Inp 850.00 NIST
Inp 835.00 NIST
Inp 840.00 NIST
Inp 849.10 NIST
Inp 849.10 NIST
Inp 849.10 NIST
Inp 849.10 NIST
Inp 849.10 NIST
Inp 849.10 NIST
Inp 847.70 NIST
Inp 848.00 NIST
Inp 843.00 NIST
Inp 846.00 NIST
Inp 850.00 NIST
Inp 852.00 NIST
Inp 855.00 NIST
Inp 859.00 NIST
Inp 834.00 NIST
Inp 848.00 NIST
Inp 844.20 NIST
Inp 851.30 NIST
Inp 844.30 NIST
Inp 879.00 NIST
Inp 830.00 NIST
Inp 836.00 NIST
Inp 841.00 NIST
Inp 846.00 NIST
Inp 876.00 NIST
Inp 884.00 NIST
Inp 892.00 NIST
Inp 868.00 NIST
Inp 847.00 NIST
Inp 853.00 NIST
Inp 859.00 NIST
Inp 843.00 NIST
Inp 840.00 NIST
Inp 844.00 NIST
Inp 848.00 NIST
Inp 864.10 NIST
Inp 844.00 NIST
Inp 853.00 NIST
Inp 858.00 NIST
Inp 843.00 NIST
Inp 850.00 NIST
Inp 851.00 NIST
Inp 855.00 NIST
Inp 857.00 NIST
Inp 868.00 NIST
Inp 855.60 NIST
Inp 850.00 NIST
Inp 850.00 NIST
Inp 866.00 NIST
Inp 862.00 NIST
Inp 879.00 NIST
Inp 871.00 NIST
Inp 868.00 NIST
Inp 869.00 NIST
Inp 854.00 NIST
Inp 864.00 NIST
Inp 864.00 NIST
Inp 893.00 NIST
Inp 850.80 NIST
Inp 876.00 NIST
Inp 856.30 NIST
Inp 855.50 NIST
Inp 853.20 NIST
Inp 856.30 NIST
Inp 857.20 NIST
Inp 839.80 NIST
Inp 868.30 NIST
Inp 872.00 NIST
Inp 860.00 NIST
Inp 857.00 NIST
Inp 865.00 NIST
Inp 866.00 NIST
Inp 865.00 NIST
Inp 866.00 NIST
Inp 856.00 NIST
Inp 847.00 NIST
Inp 855.00 NIST
Inp 849.00 NIST
Inp 834.00 NIST
Inp 860.90 NIST
Inp 836.10 NIST
Inp 841.70 NIST
Inp 846.10 NIST
Inp 846.40 NIST
Inp 861.50 NIST
Inp 853.20 NIST
Inp 856.30 NIST
Inp 857.20 NIST
Inp 856.30 NIST
Inp 855.50 NIST
Inp 844.19 NIST
Inp 844.47 NIST
Inp 858.00 NIST
Inp 845.00 NIST
Inp 858.00 NIST
Inp 844.50 NIST
Inp 844.74 NIST
Inp 845.00 NIST
Inp 864.00 NIST
Inp 855.00 NIST
Inp 848.30 NIST
Inp 856.20 NIST
Inp 848.30 NIST
Inp 848.30 NIST
Inp 856.20 NIST
Inp 845.17 NIST
Inp 845.49 NIST
Inp 848.70 NIST
Inp 844.80 NIST
Inp 844.60 NIST
Inp 841.26 NIST
Inp 844.05 NIST
Inp 845.90 NIST
Inp 857.33 NIST
Inp 860.40 NIST
Inp 862.45 NIST
Inp 843.00 NIST
Inp 877.00 NIST
Inp 858.00 NIST
Inp 863.00 NIST
Inp 865.00 NIST
Inp 846.00 NIST
Inp 870.79 NIST
Inp 845.00 NIST
Inp 858.00 NIST
Inp 859.00 NIST
Inp 852.00 NIST
Inp 855.00 NIST
Inp 858.00 NIST
Inp 864.00 NIST
Inp 869.00 NIST
Inp 853.00 NIST
Inp 859.00 NIST
Inp 847.00 NIST
Inp 857.00 NIST
Inp 858.00 NIST
Inp 858.00 NIST
Inp 859.00 NIST
Inp 859.00 NIST
Inp 847.00 NIST
Inp 850.00 NIST
Inp 858.00 NIST
Inp 859.00 NIST
Inp 863.00 NIST
Inp 864.00 NIST
Inp 843.00 NIST
Inp 843.00 NIST
Inp 844.00 NIST
Inp 844.00 NIST
Inp 842.00 NIST
Inp 842.00 NIST
Inp 842.00 NIST
Inp 852.00 NIST
Inp 852.00 NIST
Inp 852.00 NIST
Inp 852.00 NIST
Inp 852.00 NIST
Inp 852.00 NIST
Inp 853.00 NIST
Inp 835.00 NIST
Inp 847.00 NIST
Inp 831.00 NIST
Inp 838.00 NIST
Inp 845.00 NIST
Inp 849.00 NIST
Inp 842.00 NIST
Inp 856.00 NIST
Inp 836.00 NIST
Inp 850.00 NIST
Inp 859.00 NIST
Inp 852.00 NIST
Inp 857.00 NIST
Inp 849.00 NIST
Inp 858.00 NIST
Inp 864.00 NIST
Inp 845.00 NIST
Inp 863.00 NIST
Inp 851.00 NIST
Inp 851.00 NIST
Inp 866.00 NIST
Inp 845.00 NIST
Inp 861.00 NIST
Inp 846.00 NIST
Inp 863.30 NIST
Inp 868.00 NIST
Inp 829.00 NIST
Inp 846.00 NIST
Inp 886.00 NIST
Inp 859.00 NIST
Inp 866.00 NIST
Inp 860.00 NIST
Inp 865.00 NIST
Inp 878.00 NIST
Inp 855.00 NIST
Inp 849.00 NIST
Inp 847.66 NIST
Inp 851.00 NIST
Inp 847.00 NIST
Inp 868.10 NIST
Inp 843.00 NIST
Inp 846.00 NIST
Inp 850.00 NIST
Inp 852.00 NIST
Inp 838.00 NIST
Inp 841.00 NIST
Inp 842.00 NIST
Inp 856.00 NIST
Inp 869.00 NIST
Inp 843.00 NIST
Inp 850.00 NIST
Inp 848.00 NIST
Inp 844.00 NIST
Inp 844.00 NIST
Inp 844.00 NIST
Inp 868.00 NIST
Inp 846.00 NIST
Inp 850.00 NIST
Inp 835.30 NIST
Inp 837.60 NIST
Inp 840.80 NIST
Inp 843.30 NIST
Inp 845.30 NIST
Inp 847.00 NIST
Inp 835.00 NIST
Inp 837.00 NIST
Inp 840.00 NIST
Inp 843.00 NIST
Inp 845.00 NIST
Inp 846.00 NIST
Inp 842.00 NIST
Inp 841.00 NIST
Inp 845.00 NIST
Inp 842.00 NIST
Inp 860.00 NIST
Inp 850.00 NIST
Inp 864.00 NIST
Inp 866.00 NIST
Inp 852.00 NIST
Inp 840.00 NIST
Inp 867.00 NIST
Inp 857.00 NIST
Inp 868.00 NIST
Inp 851.00 NIST
Inp 870.00 NIST
Inp 869.00 NIST
Inp 850.00 NIST
Inp 871.00 NIST
Inp 855.00 NIST
Inp 893.00 NIST
Inp 855.00 NIST
Inp 868.00 NIST
Inp 868.00 NIST
Inp 851.00 NIST
Inp 859.00 NIST
Inp 866.00 NIST
Inp 851.00 NIST
Inp 839.30 NIST
Inp 869.00 NIST
Inp 879.00 NIST
Inp 858.00 NIST
Inp 848.00 NIST
Inp 868.00 NIST
Inp 853.00 NIST
Inp 846.00 NIST
Inp 848.00 NIST
Inp 854.00 NIST
Inp 861.00 NIST
Inp 854.00 NIST
Inp 872.00 NIST
Inp 858.00 NIST
Inp 851.00 NIST
Inp 858.00 NIST
Inp 854.00 NIST
Inp 854.00 NIST
Inp 863.00 NIST
Inp 846.00 NIST
Inp 854.00 NIST
Inp 846.00 NIST
Inp 847.00 NIST
Inp 861.00 NIST
Inp 860.00 NIST
Inp 859.10 NIST
Inp 863.30 NIST
Inp 862.80 NIST
Inp 862.60 NIST
Inp 847.50 NIST
Inp 867.00 NIST
Inp 844.00 NIST
Inp 870.00 NIST
Inp 846.00 NIST
Inp 830.00 NIST
Inp 840.00 NIST
Inp 846.00 NIST
Inp 846.00 NIST
Inp 848.00 NIST
Inp 849.00 NIST
Inp 864.00 NIST
Inp 843.00 NIST
Inp Outlier 118.80 NIST
Inp Outlier 118.30 NIST
Inp Outlier 134.54 NIST
Inp Outlier 118.90 NIST
Inp Outlier 129.41 NIST
Inp 858.00 NIST
Inp 845.00 NIST
I [1098.00; 1180.00]   Show Hide
I 1100.00 NIST
I 1105.00 NIST
I 1138.00 NIST
I 1131.90 NIST
I 1158.90 NIST
I 1164.30 NIST
I Outlier 1169.80 NIST
I Outlier 1175.20 NIST
I 1136.00 NIST
I 1160.90 NIST
I 1158.40 NIST
I 1159.40 NIST
I 1127.10 NIST
I 1111.10 NIST
I Outlier 1178.00 NIST
I 1154.00 NIST
I 1162.00 NIST
I Outlier 1169.00 NIST
I 1147.00 NIST
I 1126.00 NIST
I 1128.00 NIST
I 1098.00 NIST
I 1122.00 NIST
I 1116.00 NIST
I 1120.00 NIST
I 1134.00 NIST
I 1146.10 NIST
I 1123.00 NIST
I 1129.00 NIST
I 1129.00 NIST
I 1131.00 NIST
I 1127.00 NIST
I 1138.00 NIST
I 1115.00 NIST
I 1115.00 NIST
I 1130.00 NIST
I 1118.00 NIST
I 1133.00 NIST
I Outlier 1168.00 NIST
I 1138.00 NIST
I 1125.00 NIST
I 1125.00 NIST
I 1124.00 NIST
I 1138.00 NIST
I 1125.00 NIST
I 1123.00 NIST
I 1125.00 NIST
I 1129.00 NIST
I 1122.00 NIST
I 1130.00 NIST
I 1116.00 NIST
I 1128.00 NIST
I 1122.00 NIST
I 1123.00 NIST
I 1130.00 NIST
I 1132.00 NIST
I 1107.00 NIST
I 1133.00 NIST
I 1135.00 NIST
I 1125.00 NIST
I 1125.00 NIST
I 1121.00 NIST
I 1125.00 NIST
I 1125.00 NIST
I 1122.00 NIST
I 1129.00 NIST
I 1132.00 NIST
I 1132.00 NIST
I 1157.00 NIST
I Outlier 1168.00 NIST
I Outlier 1180.00 NIST
I 1135.00 NIST
I 1146.00 NIST
I 1145.00 NIST
I 1144.00 NIST
I 1146.00 NIST
I 1157.00 NIST
I 1166.00 NIST
I 1125.00 NIST
I 1135.00 NIST
I 1111.00 NIST
I 1146.00 NIST
I 1130.00 NIST
I 1130.00 NIST
I 1142.00 NIST
I 1139.00 NIST
I 1130.00 NIST
I 1116.00 NIST
I 1161.00 NIST
I 1104.00 NIST
I 1122.00 NIST
I 1122.00 NIST
I 1119.00 NIST
I 1114.00 NIST
I 1118.00 NIST
I 1141.00 NIST
I 1108.00 NIST
I 1147.00 NIST
I 1116.00 NIST
I 1126.00 NIST
I 1135.00 NIST
I 1125.00 NIST
I 1109.00 NIST
I 1126.00 NIST
I 1124.00 NIST
I 1124.00 NIST
I 1134.00 NIST
I 1139.00 NIST
I 1127.00 NIST
I 1122.00 NIST
I 1119.00 NIST
I 1161.00 NIST
I 1130.00 NIST
I 1161.00 NIST
I 1121.00 NIST
I 1125.00 NIST
I 1127.00 NIST
I 1125.00 NIST
I 1138.00 NIST
I 1161.00 NIST
I 1109.00 NIST
I 1132.00 NIST
I 1129.00 NIST
I 1111.00 NIST
I 1131.00 NIST
I 1129.00 NIST
I 1132.00 NIST
I 1129.00 NIST
I 1117.00 NIST
I 1110.00 NIST
I 1110.00 NIST
I 1117.00 NIST
I 1120.00 NIST
gas 360.60 ± 0.50 J/mol×K NIST
liquid [255.01; 256.10] J/mol×K Show Hide
liquid 255.01 J/mol×K NIST
liquid 256.10 J/mol×K NIST
Tboil [409.25; 409.35] K Show Hide
Tboil 409.34 K KDB
Tboil 409.35 K Isobaric (vapour + liquid) equilibria for sulfolane with toluene, ethylbenzene, and isopropylbenzene at 101.33 kPa
Tboil 409.35 K Isobaric (vapour + liquid) equilibria for N-formylmorpholine with ethylbenzene, n-butylbenzene, iso-propylbenzene and 1,2,4-trimethylbenzene at 101.33 kPa
Tboil 409.32 K Isobaric Vapor-Liquid Equilibium for the Binary Systems of Methyl Formate with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 101.33 kPa
Tboil 409.25 K Isobaric Vapor Liquid Equilibrium of Binary and Ternary Systems with 2-Ethoxyethanol + Ethylbenzene + Dimethyl Sulfoxide
Tc 617.15 K KDB
Tfus [178.20; 278.29] K Show Hide
Tfus 178.20 K Aq. Solubility Prediction
Tfus 178.20 K KDB
Tfus 278.29 K Phase Equilibria Study of the Binary Systems (N-Butyl-4-methylpyridinium Tosylate Ionic Liquid + Organic Solvent, or Water)
Ttriple [178.00; 178.15] K Show Hide
Ttriple 178.15 ± 0.02 K NIST
Ttriple 178.00 ± 0.30 K NIST
Vc [0.374; 0.374] m3/kmol Show Hide
Vc 0.374 m3/kmol KDB
Vc 0.374 m3/kmol NIST
Zc 0.2630460 KDB
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [159.24; 214.02] J/mol×K [373.15; 523.15] Show Hide
Cp,gas 159.24 ± 0.80 J/mol×K 373.15 NIST
Cp,gas 164.25 ± 0.33 J/mol×K 385.65 NIST
Cp,gas 169.25 ± 0.34 J/mol×K 398.15 NIST
Cp,gas 178.96 ± 0.36 J/mol×K 423.15 NIST
Cp,gas 188.28 ± 0.38 J/mol×K 448.15 NIST
Cp,gas 197.35 ± 0.39 J/mol×K 473.15 NIST
Cp,gas 205.94 ± 0.41 J/mol×K 498.15 NIST
Cp,gas 214.02 ± 0.43 J/mol×K 523.15 NIST
Cp,liquid [161.00; 186.60] J/mol×K [293.31; 303.00] Show Hide
Cp,liquid 184.80 J/mol×K 293.31 NIST
Cp,liquid 161.00 J/mol×K 295.00 NIST
Cp,liquid 181.60 J/mol×K 297.40 NIST
Cp,liquid 185.80 J/mol×K 298.00 NIST
Cp,liquid 184.50 J/mol×K 298.00 NIST
Cp,liquid 186.04 J/mol×K 298.15 NIST
Cp,liquid 185.78 J/mol×K 298.15 NIST
Cp,liquid 185.81 J/mol×K 298.15 NIST
Cp,liquid 186.60 J/mol×K 298.15 NIST
Cp,liquid 185.56 J/mol×K 298.15 NIST
Cp,liquid 185.57 J/mol×K 298.15 NIST
Cp,liquid 183.70 J/mol×K 298.50 NIST
Cp,liquid 178.70 J/mol×K 302.70 NIST
Cp,liquid 178.70 J/mol×K 302.80 NIST
Cp,liquid 181.60 J/mol×K 303.00 NIST
η [0.0003660; 0.0006793] Pa×s [293.15; 353.15] Show Hide
η 0.0006793 Pa×s 293.15 Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
η 0.0006380 Pa×s 298.15 Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η 0.0006280 Pa×s 298.15 Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
η 0.0006299 Pa×s 298.15 Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η 0.0005970 Pa×s 303.15 Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η 0.0005970 Pa×s 303.15 Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η 0.0006006 Pa×s 303.15 Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
η 0.0005986 Pa×s 303.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0005981 Pa×s 303.15 Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η 0.0005980 Pa×s 303.15 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
η 0.0005691 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0005652 Pa×s 308.15 Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η 0.0005340 Pa×s 308.15 Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for CmH2m+1(OCH2CH2)nOH (m ) 1 or 2 or 4 andn ) 1) + Benzene, + Toluene, + (o-, m-, and p-) Xylenes, + Ethylbenzene, and + Cyclohexane
η 0.0005530 Pa×s 308.15 Viscosities, Densities, and Ultrasonic Velocities of Binary Mixtures of Ethylbenzene with Ethanol, 1-Propanol, and 1-Butanol at (298.15 and 308.15)K
η 0.0005355 Pa×s 313.15 Viscosities, Densities, and Ultrasonic Velocities of 3-Pentanone + Ethylbenzene and 3-Pentanone + o-Xylene at (293.15, 303.15, and 313.15) K
η 0.0005380 Pa×s 313.15 Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η 0.0005370 Pa×s 313.15 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
η 0.0005294 Pa×s 313.15 Viscometric and Volumetric Properties of 10 Regular Binary Systems at 308.15 K and 313.15 K
η 0.0005380 Pa×s 313.15 Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η 0.0005372 Pa×s 313.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0005060 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0004805 Pa×s 323.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0004830 Pa×s 323.15 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
η 0.0004829 Pa×s 323.15 Excess Molar Volumes and Viscosities of Binary Mixtures of Sulfolane with Benzene, Toluene, Ethylbenzene, p-Xylene, o-Xylene, and m-Xylene at 303.15 and 323.15 K and Atmospheric Pressure
η 0.0004566 Pa×s 328.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0004370 Pa×s 333.15 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
η 0.0004371 Pa×s 333.15 Densities and Viscosities of Binary Mixtures of Vitamin K3 with Benzene, Toluene, Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene from (303.15 to 333.15) K
η 0.0003970 Pa×s 343.15 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
η 0.0003660 Pa×s 353.15 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
ΔfusH [9.16; 9.18] kJ/mol [178.00; 178.20] Show Hide
ΔfusH 9.16 kJ/mol 178.00 NIST
ΔfusH 9.18 kJ/mol 178.15 NIST
ΔfusH 9.16 kJ/mol 178.17 NIST
ΔfusH 9.16 kJ/mol 178.20 NIST
ΔfusH 9.16 kJ/mol 178.20 NIST
ΔvapH [35.50; 42.49] kJ/mol [294.01; 583.00] Show Hide
ΔvapH 42.49 kJ/mol 294.01 NIST
ΔvapH 40.50 ± 0.10 kJ/mol 328.00 NIST
ΔvapH 39.50 ± 0.10 kJ/mol 343.00 NIST
ΔvapH 38.60 ± 0.10 kJ/mol 358.00 NIST
ΔvapH 41.80 kJ/mol 359.00 NIST
ΔvapH 40.60 kJ/mol 360.00 NIST
ΔvapH 40.00 kJ/mol 370.00 NIST
ΔvapH 35.56 kJ/mol 409.20 KDB
ΔvapH 35.57 kJ/mol 409.30 NIST
ΔvapH 37.00 kJ/mol 434.00 NIST
ΔvapH 35.80 kJ/mol 505.50 NIST
ΔvapH 35.50 kJ/mol 583.00 NIST
Pvap [2.10; 3451.00] kPa [308.15; 613.15] Show Hide
Pvap 2.22 kPa 308.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 2.10 kPa 313.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 3.75 kPa 318.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 4.08 kPa 320.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 4.71 kPa 323.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 5.00 kPa 324.40 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 5.41 kPa 326.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 5.97 kPa 328.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 7.09 kPa 332.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 7.45 kPa 333.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 7.50 kPa 333.40 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 9.25 kPa 338.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 9.19 kPa 338.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 10.00 kPa 340.00 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 11.41 kPa 343.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 11.79 kPa 344.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 12.50 kPa 345.50 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 13.79 kPa 348.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 15.00 kPa 350.10 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 17.50 kPa 354.10 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 20.00 kPa 357.70 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 20.42 kPa 358.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 22.50 kPa 360.90 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 25.00 kPa 363.80 Isobaric Low-Pressure Vapor Liquid Equilibrium Data for Ethylbenzene + Styrene + Sulfolane and the Three Constituent Binary Systems
Pvap 26.66 kPa 365.86 Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap 29.11 kPa 368.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 40.00 kPa 377.54 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 47.75 kPa 383.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 53.33 kPa 386.69 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 53.33 kPa 386.94 Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap 66.66 kPa 394.14 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 79.99 kPa 400.51 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 79.99 kPa 400.70 Isobaric Vapor-Liquid Equilibria of the Ternary System Toluene + Ethylbenzene + Amyl Acetate
Pvap 85.64 kPa 403.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 93.32 kPa 406.12 Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
Pvap 93.13 kPa 406.23 Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
Pvap 95.30 kPa 406.95 Vapor-liquid equilibrium for the binary mixtures of dimethylsulfoxide with substituted benzenes
Pvap 250.00 kPa 447.20 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
Pvap 681.00 kPa 498.15 High-Temperature VLE for the Ethylbenzene + Quinoline System
Pvap 1027.00 kPa 523.15 High-Temperature VLE for the Ethylbenzene + Quinoline System
Pvap 1601.00 kPa 553.15 High-Temperature VLE for the Ethylbenzene + Quinoline System
Pvap 2387.00 kPa 583.15 High-Temperature VLE for the Ethylbenzene + Quinoline System
Pvap 3451.00 kPa 613.15 High-Temperature VLE for the Ethylbenzene + Quinoline System
n0 [1.49020; 1.54395]   [283.15; 303.15] Show Hide
n0 1.50129 283.15 Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
n0 1.49620 293.10 Densities and volumetric properties of N-methyl-2-pyrrolidone with aromatic hydrocarbon at different temperature
n0 1.49620 293.10 A study on densities and excess volumes in the (c-butyrolactone + aromatic hydrocarbon) system at various temperatures
n0 1.49220 293.15 Volumetric properties of binary mixtures of tributylamine with benzene derivatives and comparison with ERAS model results at temperatures from (293.15 to 333.15) K
n0 1.49620 293.15 Effect of temperature on the volumetric properties of (cyclohexanone + an aromatic hydrocarbon)
n0 1.49620 293.15 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
n0 1.50090 293.15 Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0 1.49620 293.15 A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n0 1.49600 293.15 Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
n0 1.49570 293.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
n0 1.54395 293.15 Bubble points of the binary mixtures formed by ethylbenzene with some chloroaliphatics and substituted benzenes at p = 94.7 kPa
n0 1.49550 293.15 Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
n0 1.49310 298.15 Excess Molar Volumes of (propiophenone + benzene, or toluene, or ethylbenzene, or butylbenzene) at temperatures 298.15 K and 328.15 K
n0 1.49320 298.15 Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
n0 1.49300 298.15 Experimental and correlational study of phase equilibria in aqueous mixtures of phosphoric acid with aromatic hydrocarbons at various temperatures
n0 1.49620 298.15 Densities and excess volumes of binary mixtures of N,N-dimethylformamide with aromatic hydrocarbon at different temperature
n0 1.49620 298.15 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
n0 1.49304 298.15 Effect of the Chain Length on the Aromatic Ring in the Separation of Aromatic Compounds from Methylcyclohexane Using the Ionic Liquid 1-Ethyl-3-methylpyridinium Ethylsulfate
n0 1.49320 298.15 KDB
n0 1.49304 298.15 (Liquid + liquid) equilibrium data for the ternary systems (cycloalkane + ethylbenzene + 1-ethyl-3-methylimidazolium ethylsulfate) at T = 298.15 K and atmospheric pressure
n0 1.49304 298.15 Liquid Liquid Extraction of Aromatic Compounds from Cycloalkanes Using 1-Butyl-3-methylimidazolium Methylsulfate Ionic Liquid
n0 1.49320 298.15 Bubble temperature measurements on seven binary mixtures formed by ethylbenzene at 94.7 kPa
n0 1.49316 298.15 Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n0 1.49304 298.15 Density, Speed of Sound, and Refractive Index of the Binary Systems Cyclohexane (1) or Methylcyclohexane (1) or Cyclo-octane (1) with Benzene (2), Toluene (2), and Ethylbenzene (2) at Two Temperatures
n0 1.49304 298.15 Liquid-Liquid Equilibrium for Ternary Mixtures of Hexane + Aromatic Compounds + [EMpy][ESO4] at T = 298.15 K
n0 1.49020 303.15 Densities, Viscosities, and Refractive Indices of Binary Mixtures of Anisole with Benzene, Methylbenzene, Ethylbenzene, Propylbenzene, and Butylbenzene at (293.15 and 303.15) K
ρl [794.20; 875.69] kg/m3 [283.15; 373.15] Show Hide
ρl 875.69 kg/m3 283.15 The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl 871.31 kg/m3 288.15 Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
ρl 871.33 kg/m3 288.15 Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
ρl 871.30 kg/m3 288.15 The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl 867.00 kg/m3 293.00 KDB
ρl 867.10 kg/m3 293.10 Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
ρl 866.95 kg/m3 293.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 867.10 kg/m3 293.15 Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl 866.54 kg/m3 293.15 Isobaric vapor liquid equilibium for the binary systerms of 1-butanol with o-xylene, m-xylene, p-xylene, and ethylbenzene at 101.33 kPa
ρl 867.10 kg/m3 293.15 Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl 866.90 kg/m3 293.15 The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl 867.20 kg/m3 293.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 862.50 kg/m3 298.15 Excess Molar Entalpies of Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene, or Ethyl Benzoate at 298.15 K
ρl 862.58 kg/m3 298.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 862.50 kg/m3 298.15 Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes and Aromatic Compounds at T = 313.15 K
ρl 862.55 kg/m3 298.15 Excess Enthalpies of Chloroalkylbenzene + Alkylbenzene Mixtures
ρl 862.37 kg/m3 298.15 Experimental Study of the Dynamic Viscosity Deviations in the Binary Systems: Hexane + Ethylbenzene, + o-Xylene, + m-Xylene, + p-Xylene at 298.15 K
ρl 862.57 kg/m3 298.15 Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
ρl 862.70 kg/m3 298.15 Densities and Kinematic Viscosities of One Quinary Regular Liquid System and Its Five Quaternary Sub-Systems at Temperatures (293.15 and 298.15) K
ρl 862.59 kg/m3 298.15 Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
ρl 862.55 kg/m3 298.15 Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
ρl 862.43 kg/m3 298.15 Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
ρl 862.70 kg/m3 298.15 Densities and Kinematic Viscosities of a Quinary Regular Liquid System and Its Five Quaternary Subsystems at 293.15A K and 298.15A K
ρl 862.51 kg/m3 298.15 Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
ρl 862.50 kg/m3 298.15 Thermodynamics of Ternary Liquid Mixtures Containing Toluene, Ethylbenzene, and Chlorobenzene
ρl 862.50 kg/m3 298.15 Excess Molar Enthalpies for Dimethyl Carbonate with o-Xylene, m-Xylene, p-Xylene, Ethylbenzene or Ethyl Benzoate at 298.15 K and 10.2 MPa
ρl 862.55 kg/m3 298.15 Thermodynamic study of 1,1,2,2-tetrachloroethane + hydrocarbon mixtures I. Excess and solvation enthalpies
ρl 862.51 kg/m3 298.15 Phase behavior of ternary mixtures {aliphatic hydrocarbon + aromatic hydrocarbon + ionic liquid}: Experimental LLE data and their modeling by COSMO-RS
ρl 862.70 kg/m3 298.15 Isobaric Vapor-Liquid Equilibrium for Binary and Ternary Systems of 2-Methoxyethanol, Ethylbenzene, and Dimethyl Sulfoxide at 100.00 kPa
ρl 862.50 kg/m3 298.15 Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl 862.97 kg/m3 298.15 Phase behaviour of tricyanomethanide-based ionic liquids with alcohols and hydrocarbons
ρl 862.58 kg/m3 298.15 The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl 862.51 kg/m3 298.15 Liquid Phase Equilibria of Aqueous Mixtures of Carboxylic Acids (C1-C4) with Ethylbenzene: Thermodynamic and Mathematical Modeling
ρl 862.51 kg/m3 298.15 (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
ρl 862.97 kg/m3 298.15 Phase behaviour of ionic liquid 1-butyl-1-methylpyrrolidinium tris(pentafluoroethyl)trifluorophosphate with alcohols, water and aromatic hydrocarbons
ρl 862.59 kg/m3 298.15 Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
ρl 862.57 kg/m3 298.15 Isobaric Vapor Liquid Equilibrium for the Binary Systems of Diethyl Carbonate with Xylene Isomers and Ethylbenzene at 101.33 kPa
ρl 862.70 kg/m3 298.15 The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl 863.54 kg/m3 298.15 Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
ρl 858.30 kg/m3 303.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 858.10 kg/m3 303.15 Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
ρl 858.16 kg/m3 303.15 The density, refractive index, and thermodynamic behaviour of binary mixtures of 1,3-Diethenyl-1,1,3,3-tetramethyldisiloxane with aromatic hydrocarbons
ρl 858.15 kg/m3 303.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 853.71 kg/m3 308.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 853.75 kg/m3 308.15 Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
ρl 853.80 kg/m3 308.15 The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl 853.77 kg/m3 308.15 Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
ρl 853.61 kg/m3 308.15 Acoustic and thermodynamic properties of binary mixtures of 1-nonanol with o-xylene, m-xylene, p-xylene, ethylbenzene and mesitylene at T = (298.15 and 308.15) K
ρl 853.68 kg/m3 308.15 Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
ρl 849.30 kg/m3 313.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 849.29 kg/m3 313.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 849.29 kg/m3 313.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 849.26 kg/m3 313.15 Experimental density, viscosity, interfacial tension and water solubility of ethyl benzene - a-methyl benzyl alcohol - water system
ρl 844.80 kg/m3 318.15 The density, the refractive index and the adjustment of the excess thermodynamic properties by means of the multiple linear regression method for the ternary system ethylbenzene-octane-propylbenzene
ρl 844.70 kg/m3 318.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 844.89 kg/m3 318.15 Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
ρl 844.87 kg/m3 318.15 Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
ρl 840.28 kg/m3 323.15 The physicochemical properties of 1,3,5-trimethyl-1,3,5-tris(3,3,3-trifluoropropyl)cyclotrisiloxane with various aromatic hydrocarbons at T = (308.15 to 323.15) K
ρl 840.30 kg/m3 323.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 840.38 kg/m3 323.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 835.93 kg/m3 328.15 Effect of temperature and composition on the density, refractive index, and excess quantities of binary mixtures of 2,4,6,8-tetramethyl-2,4,6,8- tetraethenylcyclotetrasiloxane with aromatic hydrocarbons
ρl 835.94 kg/m3 328.15 Thermophysical properties of binary mixtures of triethoxysilane, methyltriethoxysilane, vinyltriethoxysilane and 3-mercaptopropyltriethoxysilane with ethylbenzene at various temperatures
ρl 831.40 kg/m3 333.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 831.20 kg/m3 333.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 822.30 kg/m3 343.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 822.10 kg/m3 343.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 813.10 kg/m3 353.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 803.70 kg/m3 363.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ρl 794.20 kg/m3 373.15 Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of n-Hexadecane + Ethylbenzene or + Toluene at (293.15 to 373.15) K and 0.1 MPa
ΔfusS [51.43; 51.54] J/mol×K [178.00; 178.17] Show Hide
ΔfusS 51.48 J/mol×K 178.00 NIST
ΔfusS 51.54 J/mol×K 178.15 NIST
ΔfusS 51.43 J/mol×K 178.17 NIST
csound,fluid [1213.59; 1360.73] m/s [288.15; 323.15] Show Hide
csound,fluid 1359.11 m/s 288.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid 1360.73 m/s 288.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1349.91 m/s 290.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1339.40 m/s 293.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1340.00 m/s 293.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1328.86 m/s 295.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1318.36 m/s 298.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1319.00 m/s 298.15 Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid 1316.23 m/s 298.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
csound,fluid 1307.90 m/s 300.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1298.00 m/s 303.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1297.48 m/s 303.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1287.09 m/s 305.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1276.00 m/s 308.15 Densities, Speeds of Sound, Excess Molar Volumes, and Excess Isentropic Compressibilities at T = (298.15 and 308.15) K for Methyl Methacrylate + 1-Alkanols (1-Butanol, 1-Pentanol, and 1-Heptanol) + Cyclohexane, + Benzene, + Toluene, + p-Xylene, and + Ethylbenzene
csound,fluid 1276.75 m/s 308.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1266.54 m/s 310.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1256.29 m/s 313.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1257.00 m/s 313.15 Densities, Speeds of Sound, and Isentropic Compressibilities of Binary Mixtures of {Alkan-1-ols + 1,2-Dimethylbenzene, or 1,3-Dimethylbenzene, or 1,4-Dimethylbenzene, or Ethylbenzene} at (293.15, 303.15, and 313.15) K
csound,fluid 1246.12 m/s 315.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1236.06 m/s 318.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1226.09 m/s 320.65 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1216.34 m/s 323.15 Influence of Temperature on Thermodynamic Properties of Methyl t-Butyl Ether (MTBE)+Gasoline Additives
csound,fluid 1213.59 m/s 323.15 Temperature influence on mixing properties of {ethyl tert-butyl ether (ETBE) + gasoline additives}
γ [0.03; 0.03] N/m [293.20; 323.15] Show Hide
γ 0.03 N/m 293.20 KDB
γ 0.03 N/m 298.15 Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ 0.03 N/m 303.15 Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ 0.03 N/m 303.15 Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ 0.03 N/m 308.15 Densities and Surface Tensions of Propyl Acetate + Xylenes or + Ethylbenzene from (298.15 to 308.15) K
γ 0.03 N/m 313.15 Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
γ 0.03 N/m 323.15 Thermo Physical Properties of 4-Hydroxy 4-Methyl Pentanone with Nitrobenzene or Ethyl Benzene at Temperatures of (303.15, 313.15, and 323.15) K and a Pressure of 0.1 MPa
ΔvapS 144.50 J/mol×K 294.01 NIST
λ [0.12; 0.14] W/m×K [258.00; 329.66] Show Hide
λ 0.14 W/m×K 258.00 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.14 W/m×K 258.29 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.14 W/m×K 258.50 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.34 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.65 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.88 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 295.86 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 296.19 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 296.42 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 312.38 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 312.72 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 312.96 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 329.05 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 329.41 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 329.66 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboil 408.75 K 95.30 Excess enthalpies of dimethylsulfoxide with substituted benzenes at 298.15K

Datasets

  1. Viscosity, Pa*s (1)
  2. Refractive index (Na D-line) (1)
  3. Mass density, kg/m3 (1)

Viscosity, Pa*s

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
253.23 100.00 0.0012
253.22 1000.00 0.0012
253.21 5000.00 0.0013
253.22 10000.00 0.0013
253.24 15000.00 0.0014
253.23 20000.00 0.0014
253.23 25000.00 0.0015
253.24 30000.00 0.0015
253.22 35000.00 0.0016
263.22 100.00 0.0010
263.22 1000.00 0.0010
263.21 5000.00 0.0011
263.20 10000.00 0.0011
263.20 15000.00 0.0012
263.21 20000.00 0.0012
263.21 25000.00 0.0013
263.22 30000.00 0.0013
263.21 35000.00 0.0014
273.21 100.00 0.0009
273.17 1000.00 0.0009
273.15 5000.00 0.0009
273.18 10000.00 0.0010
273.19 15000.00 0.0010
273.15 20000.00 0.0010
273.16 25000.00 0.0011
273.15 30000.00 0.0011
273.15 35000.00 0.0012
283.16 100.00 0.0008
283.13 1000.00 0.0008
283.16 5000.00 0.0008
283.14 10000.00 0.0008
283.17 15000.00 0.0009
283.15 20000.00 0.0009
283.17 25000.00 0.0009
283.16 30000.00 0.0010
283.16 35000.00 0.0010
293.26 100.00 0.0007
293.20 1000.00 0.0007
293.18 5000.00 0.0007
293.24 10000.00 0.0007
293.23 15000.00 0.0008
293.24 20000.00 0.0008
293.22 25000.00 0.0008
293.24 30000.00 0.0008
293.26 35000.00 0.0009
303.15 100.00 0.0006
303.17 1000.00 0.0006
303.18 5000.00 0.0006
303.20 10000.00 0.0006
303.19 15000.00 0.0007
303.17 20000.00 0.0007
303.18 25000.00 0.0007
303.19 30000.00 0.0008
303.18 35000.00 0.0008
313.12 100.00 0.0005
313.12 1000.00 0.0005
313.11 5000.00 0.0006
313.10 10000.00 0.0006
313.12 15000.00 0.0006
313.09 20000.00 0.0006
313.10 25000.00 0.0006
313.08 30000.00 0.0007
313.10 35000.00 0.0007
322.97 100.00 0.0005
322.98 1000.00 0.0005
322.98 5000.00 0.0005
322.98 10000.00 0.0005
322.98 15000.00 0.0005
322.97 20000.00 0.0006
322.98 25000.00 0.0006
322.98 30000.00 0.0006
322.98 35000.00 0.0006
332.91 100.00 0.0004
332.92 1000.00 0.0004
332.91 5000.00 0.0005
332.92 10000.00 0.0005
332.92 15000.00 0.0005
332.92 20000.00 0.0005
332.92 25000.00 0.0005
332.92 30000.00 0.0006
332.92 35000.00 0.0006
342.81 100.00 0.0004
342.80 1000.00 0.0004
342.81 5000.00 0.0004
342.80 10000.00 0.0004
342.80 15000.00 0.0005
342.80 20000.00 0.0005
342.80 25000.00 0.0005
342.80 30000.00 0.0005
342.80 35000.00 0.0005
352.73 100.00 0.0004
352.73 1000.00 0.0004
352.72 5000.00 0.0004
352.73 10000.00 0.0004
352.73 15000.00 0.0004
352.72 20000.00 0.0004
352.73 25000.00 0.0004
352.73 30000.00 0.0005
352.72 35000.00 0.0005
362.66 100.00 0.0003
362.66 1000.00 0.0003
362.66 5000.00 0.0004
362.67 10000.00 0.0004
362.66 15000.00 0.0004
362.66 20000.00 0.0004
362.66 25000.00 0.0004
362.66 30000.00 0.0004
362.67 35000.00 0.0004
372.61 100.00 0.0003
372.60 1000.00 0.0003
372.59 5000.00 0.0003
372.59 10000.00 0.0003
372.59 15000.00 0.0004
372.59 20000.00 0.0004
372.59 25000.00 0.0004
372.59 30000.00 0.0004
372.59 35000.00 0.0004
Reference

Refractive index (Na D-line)

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Refractive index (Na D-line) - Liquid
93.00 298.15 1.493
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
292.25 100.00 867.0
292.25 5000.00 870.8
292.25 9900.00 874.0
292.25 19700.00 881.3
292.25 29500.00 887.1
292.25 39300.00 893.0
292.25 49100.00 898.5
292.25 58900.00 903.8
313.45 100.00 849.1
313.45 5000.00 853.1
313.45 19700.00 864.4
313.45 29500.00 871.4
313.45 39300.00 877.6
313.45 49100.00 883.6
313.45 58900.00 889.4
336.55 100.00 828.7
336.55 5000.00 833.6
336.55 9900.00 838.5
336.55 19700.00 845.8
336.55 29500.00 854.0
336.55 39300.00 860.9
336.55 49100.00 867.8
336.55 58900.00 873.6
358.81 100.00 808.4
358.81 5000.00 814.5
358.81 9900.00 820.0
358.81 19700.00 827.6
358.81 29500.00 836.8
358.81 39300.00 844.8
358.81 49100.00 852.4
358.81 58900.00 858.6
382.95 5000.00 793.0
382.95 9900.00 799.0
382.95 19700.00 808.1
382.95 29500.00 818.2
382.95 39300.00 827.1
382.95 49100.00 835.1
382.95 58900.00 842.5
408.05 5000.00 770.4
408.05 9900.00 777.3
408.05 19700.00 788.5
408.05 29500.00 799.7
408.05 39300.00 809.5
408.05 49100.00 817.9
408.05 58900.00 826.0
434.45 5000.00 746.0
434.45 9900.00 754.4
434.45 19700.00 768.1
434.45 29500.00 780.5
434.45 39300.00 791.0
434.45 49100.00 800.4
434.45 58900.00 808.6
461.85 5000.00 718.6
461.85 9900.00 728.8
461.85 19700.00 746.2
461.85 29500.00 760.0
461.85 39300.00 771.7
461.85 49100.00 782.3
461.85 58900.00 791.0
490.15 5000.00 687.0
490.15 9900.00 700.0
490.15 19700.00 720.9
490.15 29500.00 737.2
490.15 39300.00 750.7
490.15 49100.00 762.9
490.15 58900.00 773.2
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [297.90; 436.98] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.44625e+01
Coefficient B-3.59099e+03
Coefficient C-4.45680e+01
Temperature range, min.297.90
Temperature range, max.436.98
Pvap 1.33 kPa 297.90 Calculated Property
Pvap 3.01 kPa 313.35 Calculated Property
Pvap 6.23 kPa 328.81 Calculated Property
Pvap 11.94 kPa 344.26 Calculated Property
Pvap 21.50 kPa 359.71 Calculated Property
Pvap 36.62 kPa 375.17 Calculated Property
Pvap 59.47 kPa 390.62 Calculated Property
Pvap 92.68 kPa 406.07 Calculated Property
Pvap 139.26 kPa 421.53 Calculated Property
Pvap 202.65 kPa 436.98 Calculated Property
Pvap [4.05e-06; 3587.82] kPa [178.15; 617.17] KDB Vapor Pressure Data Show Hide
Equationln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A7.97937e+01
Coefficient B-7.63808e+03
Coefficient C-9.55398e+00
Coefficient D5.65318e-06
Temperature range, min.178.15
Temperature range, max.617.17
Pvap 4.05e-06 kPa 178.15 Calculated Property
Pvap 4.51e-03 kPa 226.93 Calculated Property
Pvap 0.31 kPa 275.71 Calculated Property
Pvap 4.99 kPa 324.49 Calculated Property
Pvap 34.37 kPa 373.27 Calculated Property
Pvap 140.91 kPa 422.05 Calculated Property
Pvap 413.38 kPa 470.83 Calculated Property
Pvap 971.25 kPa 519.61 Calculated Property
Pvap 1964.29 kPa 568.39 Calculated Property
Pvap 3587.82 kPa 617.17 Calculated Property

Similar Compounds

Ethylbenzene-d10. Benzene, 1,4-diethyl-. Benzene, 1-ethyl-4-methyl-. 1-Phenylethyl radical. Benzene, 1,3-diethyl-. Benzene, 1-ethyl-3-methyl-. Benzene, (2-bromoethyl)-. Benzene, (2-fluoroethyl)-. Benzene, (2-chloroethyl)-. Benzene, (2-iodoethyl)-. Naphthalene, 2-ethyl-. 4-Ethylphenylacetonitrile. Benzeneacetaldehyde. Phenanthrene, 2-ethyl-. Anthracene, 2-ethyl-.

Find more compounds similar to Ethylbenzene.

Mixtures

Find more mixtures with Ethylbenzene.

Sources

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