Chemical Properties of o-Xylene (CAS 95-47-6)

o-Xylene

InChI
InChI=1S/C8H10/c1-7-5-3-4-6-8(7)2/h3-6H,1-2H3
InChI Key
CTQNGGLPUBDAKN-UHFFFAOYSA-N
Formula
C8H10
SMILES
Cc1ccccc1C
Molecular Weight1
106.17
CAS
95-47-6
Other Names
  • 1,2-Dimethylbenzene
  • 1,2-Xylene
  • 1,2-dimethyl-benzene ( o-xylene)
  • 2-Methyltoluene
  • 3,4-Xylene
  • Benzene, 1,2-dimethyl-
  • NSC 60920
  • o-Dimethylbenzene
  • o-Methyltoluene
  • o-Xylol
  • ortho-Xylene
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Contents

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

Physical Properties

Property Value Unit Source
ω 0.3100 KDB
PAff [791.20; 796.00] kJ/mol Show Hide
PAff 796.00 kJ/mol NIST
PAff 791.20 kJ/mol NIST
PAff 793.50 ± 1.70 kJ/mol NIST
Tig 738.15 K KDB
BasG [765.30; 772.10] kJ/mol Show Hide
BasG 768.30 kJ/mol NIST
BasG 765.30 kJ/mol NIST
BasG 772.10 ± 2.20 kJ/mol NIST
Δcliquid [-4581.40; -4551.48] kJ/mol Show Hide
Δcliquid -4551.48 ± 0.50 kJ/mol NIST
Δcliquid -4552.90 ± 1.00 kJ/mol NIST
Δcliquid -4567.60 kJ/mol NIST
Δcliquid -4581.40 kJ/mol NIST
Cp,liquid 187.28 J/mol×K Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ 0.50 debye KDB
η [0.0007680; 0.0007690] Pa×s Show Hide
η 0.0007680 Pa×s Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 2-Butanone at 298.15 K
η 0.0007690 Pa×s Viscosities, Densities, and Speeds of Sound of Binary Mixtures of o-Xylene, m-Xylene, p-Xylene, and Isopropylbenzene with 4-Methylpentan-2-one at 298.15 K
SProt 36.90 J/mol×K NIST
LFL 1.10 % in Air KDB
UFL 7.00 % in Air KDB
Tflash,cc 297.04 K KDB
Tflash,oc 290.37 K KDB
Δf 122.20 kJ/mol KDB
Rg 3.7890 KDB
Δc,grossH 4552.86 kJ/mol KDB
Δc,netH 4332.784 kJ/mol KDB
Δfgas [19.00; 19.00] kJ/mol Show Hide
Δfgas 19.00 kJ/mol KDB
Δfgas 19.00 ± 1.10 kJ/mol NIST
Δfliquid -24.40 ± 1.10 kJ/mol NIST
Δfus 10.13 kJ/mol Joback Calculated Property
Δvap 44.77 kJ/mol Relay (1.0) Calculated Property
IE [8.45; 8.85] eV Show Hide
IE 8.56 ± 0.04 eV NIST
IE 8.56 ± 0.01 eV NIST
IE Outlier 8.85 ± 0.05 eV NIST
IE 8.45 ± 0.02 eV NIST
IE 8.70 eV NIST
IE 8.60 ± 0.10 eV NIST
IE 8.61 eV NIST
IE 8.55 eV NIST
IE 8.56 ± 0.01 eV NIST
IE 8.56 ± 0.02 eV NIST
IE 8.58 ± 0.01 eV NIST
IE 8.56 eV NIST
IE 8.57 ± 0.03 eV NIST
IE 8.57 eV NIST
IE 8.75 ± 0.03 eV NIST
log10WS [-2.80; -2.80]   Show Hide
log10WS -2.80 Estimated Solubility
log10WS -2.80 Aq. Solubility Prediction
logPoct/wat 2.303 Crippen Calculated Property
McVol 99.820 ml/mol McGowan Calculated Property
NFPA Fire 3 KDB
NFPA Health 2 KDB
Pc 3732.00 kPa KDB
ρc [286.54; 287.71] kg/m3 Show Hide
ρc 286.65 ± 4.25 kg/m3 NIST
ρc 286.54 ± 5.31 kg/m3 NIST
ρc 287.71 ± 4.25 kg/m3 NIST
Inp [128.10; 933.00]   Show Hide
Inp 879.40 NIST
Inp 874.60 NIST
Inp 875.70 NIST
Inp 873.40 NIST
Inp 871.90 NIST
Inp 874.20 NIST
Inp 878.70 NIST
Inp 918.00 NIST
Inp 908.30 NIST
Inp 915.10 NIST
Inp 874.17 NIST
Inp 874.10 NIST
Inp 874.64 NIST
Inp 900.00 NIST
Inp 868.00 NIST
Inp 870.90 NIST
Inp 873.80 NIST
Inp 876.70 NIST
Inp 879.50 NIST
Inp 882.40 NIST
Inp 885.20 NIST
Inp 877.40 NIST
Inp 878.32 NIST
Inp 890.30 NIST
Inp 880.00 NIST
Inp 892.90 NIST
Inp 877.60 NIST
Inp 877.80 NIST
Inp 878.00 NIST
Inp 878.10 NIST
Inp 877.40 NIST
Inp 884.00 NIST
Inp 877.00 NIST
Inp 878.00 NIST
Inp 889.00 NIST
Inp 889.00 NIST
Inp 878.00 NIST
Inp 889.80 NIST
Inp 895.60 NIST
Inp 888.80 NIST
Inp 888.80 NIST
Inp 889.80 NIST
Inp 887.30 NIST
Inp 888.00 NIST
Inp 889.00 NIST
Inp 874.00 NIST
Inp 879.60 NIST
Inp 889.00 NIST
Inp 875.00 NIST
Inp 868.30 NIST
Inp 874.00 NIST
Inp 895.00 NIST
Inp 914.00 NIST
Inp 889.00 NIST
Inp 889.00 NIST
Inp 889.00 NIST
Inp 889.00 NIST
Inp 893.00 NIST
Inp 885.00 NIST
Inp 884.00 NIST
Inp 868.40 NIST
Inp 905.00 NIST
Inp 881.00 NIST
Inp 890.00 NIST
Inp 888.00 NIST
Inp 891.00 NIST
Inp 885.00 NIST
Inp 884.00 NIST
Inp 882.00 NIST
Inp 877.60 NIST
Inp 878.10 NIST
Inp 882.20 NIST
Inp 900.00 NIST
Inp 885.00 NIST
Inp 890.00 NIST
Inp 896.00 NIST
Inp 903.00 NIST
Inp 844.00 NIST
Inp 880.80 NIST
Inp 883.00 NIST
Inp 890.30 NIST
Inp 896.40 NIST
Inp 903.20 NIST
Inp 895.00 NIST
Inp 880.00 NIST
Inp 868.90 NIST
Inp 880.30 NIST
Inp 880.50 NIST
Inp 880.80 NIST
Inp 881.50 NIST
Inp 875.60 NIST
Inp 875.90 NIST
Inp 879.90 NIST
Inp 880.80 NIST
Inp 874.30 NIST
Inp 874.50 NIST
Inp 880.80 NIST
Inp 883.00 NIST
Inp 886.00 NIST
Inp 880.00 NIST
Inp 880.00 NIST
Inp 872.00 NIST
Inp 874.00 NIST
Inp 877.26 NIST
Inp 896.00 NIST
Inp 900.00 NIST
Inp 881.00 NIST
Inp 870.00 NIST
Inp 875.00 NIST
Inp 878.90 NIST
Inp 883.70 NIST
Inp 886.00 NIST
Inp 877.00 NIST
Inp 885.00 NIST
Inp 889.00 NIST
Inp 891.00 NIST
Inp 894.00 NIST
Inp 898.00 NIST
Inp 870.70 NIST
Inp 903.00 NIST
Inp 880.00 NIST
Inp 883.00 NIST
Inp 888.40 NIST
Inp 888.10 NIST
Inp 880.10 NIST
Inp 864.00 NIST
Inp 871.00 NIST
Inp 877.00 NIST
Inp 882.00 NIST
Inp 918.00 NIST
Inp 926.00 NIST
Inp 933.00 NIST
Inp 911.00 NIST
Inp 885.00 NIST
Inp 893.00 NIST
Inp 882.00 NIST
Inp 908.00 NIST
Inp 893.20 NIST
Inp 891.00 NIST
Inp 884.00 NIST
Inp 875.00 NIST
Inp 881.00 NIST
Inp 881.00 NIST
Inp 887.00 NIST
Inp 887.00 NIST
Inp 910.00 NIST
Inp 883.80 NIST
Inp 880.00 NIST
Inp 887.00 NIST
Inp 894.00 NIST
Inp 893.00 NIST
Inp 896.00 NIST
Inp 886.00 NIST
Inp 894.00 NIST
Inp 862.00 NIST
Inp 894.00 NIST
Inp 881.80 NIST
Inp 896.00 NIST
Inp 888.00 NIST
Inp 889.90 NIST
Inp 891.20 NIST
Inp 871.00 NIST
Inp 898.40 NIST
Inp 890.00 NIST
Inp 863.00 NIST
Inp 888.00 NIST
Inp 863.00 NIST
Inp 877.70 NIST
Inp 890.00 NIST
Inp 886.00 NIST
Inp 897.00 NIST
Inp 876.00 NIST
Inp 892.10 NIST
Inp 867.90 NIST
Inp 872.30 NIST
Inp 876.70 NIST
Inp 877.00 NIST
Inp 850.00 NIST
Inp 888.00 NIST
Inp 889.90 NIST
Inp 891.20 NIST
Inp 875.31 NIST
Inp 875.68 NIST
Inp 875.00 NIST
Inp 875.88 NIST
Inp 875.89 NIST
Inp 876.00 NIST
Inp 888.00 NIST
Inp 887.00 NIST
Inp 881.30 NIST
Inp 875.60 NIST
Inp 874.60 NIST
Inp 870.77 NIST
Inp 874.14 NIST
Inp 876.31 NIST
Inp 887.70 NIST
Inp 891.29 NIST
Inp 893.63 NIST
Inp 875.00 NIST
Inp 875.12 NIST
Inp 874.00 NIST
Inp 897.40 NIST
Inp 900.00 NIST
Inp 888.00 NIST
Inp 894.00 NIST
Inp 896.00 NIST
Inp 903.66 NIST
Inp 877.00 NIST
Inp 895.00 NIST
Inp 890.00 NIST
Inp 881.00 NIST
Inp 884.00 NIST
Inp 889.00 NIST
Inp 890.00 NIST
Inp 895.00 NIST
Inp 896.00 NIST
Inp 883.00 NIST
Inp 865.00 NIST
Inp 874.00 NIST
Inp 874.00 NIST
Inp 880.00 NIST
Inp 894.00 NIST
Inp 838.00 NIST
Inp 875.00 NIST
Inp 888.00 NIST
Inp 895.00 NIST
Inp 894.00 NIST
Inp 883.00 NIST
Inp 889.00 NIST
Inp 881.00 NIST
Inp 890.00 NIST
Inp 891.00 NIST
Inp 893.00 NIST
Inp 896.00 NIST
Inp 883.00 NIST
Inp 898.00 NIST
Inp 901.00 NIST
Inp 898.00 NIST
Inp 876.00 NIST
Inp 882.00 NIST
Inp 884.00 NIST
Inp 885.00 NIST
Inp 878.00 NIST
Inp 868.00 NIST
Inp 901.00 NIST
Inp 901.00 NIST
Inp 871.00 NIST
Inp 873.00 NIST
Inp 890.00 NIST
Inp 899.00 NIST
Inp 896.00 NIST
Inp 896.00 NIST
Inp 902.00 NIST
Inp 887.00 NIST
Inp 877.74 NIST
Inp 896.00 NIST
Inp 881.00 NIST
Inp 877.00 NIST
Inp 896.00 NIST
Inp 898.00 NIST
Inp 860.00 NIST
Inp 896.50 NIST
Inp 850.00 NIST
Inp 879.00 NIST
Inp 885.00 NIST
Inp 883.00 NIST
Inp 869.00 NIST
Inp 872.00 NIST
Inp 892.00 NIST
Inp 879.00 NIST
Inp 878.00 NIST
Inp 876.00 NIST
Inp 876.00 NIST
Inp 889.00 NIST
Inp 875.60 NIST
Inp 870.50 NIST
Inp 873.40 NIST
Inp 877.30 NIST
Inp 880.10 NIST
Inp 882.50 NIST
Inp 870.00 NIST
Inp 873.00 NIST
Inp 876.00 NIST
Inp 879.00 NIST
Inp 882.00 NIST
Inp 877.00 NIST
Inp 871.00 NIST
Inp 875.00 NIST
Inp 854.00 NIST
Inp 880.00 NIST
Inp 879.00 NIST
Inp 894.00 NIST
Inp 896.00 NIST
Inp 905.00 NIST
Inp 894.00 NIST
Inp 891.00 NIST
Inp 896.00 NIST
Inp 870.00 NIST
Inp 878.00 NIST
Inp 872.00 NIST
Inp 888.00 NIST
Inp 910.00 NIST
Inp 889.00 NIST
Inp 884.00 NIST
Inp 882.00 NIST
Inp 898.00 NIST
Inp 869.52 NIST
Inp 903.00 NIST
Inp 904.00 NIST
Inp 890.00 NIST
Inp 878.00 NIST
Inp 901.00 NIST
Inp 883.00 NIST
Inp 875.00 NIST
Inp 878.00 NIST
Inp 886.00 NIST
Inp 892.00 NIST
Inp 906.00 NIST
Inp 895.00 NIST
Inp 882.00 NIST
Inp 890.00 NIST
Inp 855.00 NIST
Inp 875.00 NIST
Inp 886.00 NIST
Inp 875.00 NIST
Inp 881.00 NIST
Inp 892.00 NIST
Inp 895.00 NIST
Inp 888.20 NIST
Inp 896.40 NIST
Inp 894.90 NIST
Inp 894.80 NIST
Inp 884.00 NIST
Inp 866.00 NIST
Inp 876.00 NIST
Inp 884.00 NIST
Inp 900.00 NIST
Inp 879.00 NIST
Inp 885.00 NIST
Inp 884.00 NIST
Inp 900.00 NIST
Inp 880.00 NIST
Inp Outlier 128.10 NIST
Inp Outlier 128.40 NIST
Inp Outlier 130.67 NIST
Inp 883.80 NIST
I [1155.00; 1234.30]   Show Hide
I 1221.00 NIST
I Outlier 1234.30 NIST
I 1174.00 NIST
I 1174.00 NIST
I 1174.60 NIST
I 1188.70 NIST
I 1191.40 NIST
I 1193.00 NIST
I 1200.00 NIST
I 1186.00 NIST
I 1209.84 NIST
I 1215.66 NIST
I 1221.09 NIST
I 1192.98 NIST
I 1198.32 NIST
I 1204.40 NIST
I 1185.70 NIST
I 1191.00 NIST
I 1183.90 NIST
I 1164.90 NIST
I Outlier 1230.00 NIST
I Outlier 1232.00 NIST
I 1210.00 NIST
I 1218.00 NIST
I Outlier 1227.00 NIST
I 1201.00 NIST
I 1184.00 NIST
I 1181.00 NIST
I 1185.00 NIST
I 1185.00 NIST
I 1191.00 NIST
I 1178.00 NIST
I 1183.00 NIST
I 1171.00 NIST
I 1195.00 NIST
I 1159.00 NIST
I 1204.40 NIST
I 1187.00 NIST
I 1174.00 NIST
I 1187.00 NIST
I 1174.00 NIST
I 1189.00 NIST
I 1192.00 NIST
I 1175.00 NIST
I 1188.00 NIST
I 1177.00 NIST
I 1184.00 NIST
I 1187.00 NIST
I 1190.00 NIST
I 1169.00 NIST
I 1183.00 NIST
I 1181.00 NIST
I 1191.00 NIST
I 1190.00 NIST
I 1191.00 NIST
I 1176.00 NIST
I 1190.00 NIST
I 1175.00 NIST
I 1176.00 NIST
I 1189.00 NIST
I 1193.00 NIST
I 1208.00 NIST
I 1186.00 NIST
I 1182.00 NIST
I 1175.00 NIST
I 1186.00 NIST
I 1186.00 NIST
I 1190.00 NIST
I 1188.00 NIST
I 1191.00 NIST
I 1216.00 NIST
I Outlier 1229.00 NIST
I 1189.00 NIST
I 1203.00 NIST
I 1202.00 NIST
I 1198.00 NIST
I 1201.00 NIST
I 1213.00 NIST
I Outlier 1225.00 NIST
I 1178.00 NIST
I 1188.00 NIST
I 1165.00 NIST
I 1204.00 NIST
I 1159.00 NIST
I 1177.00 NIST
I 1189.00 NIST
I 1197.00 NIST
I 1173.00 NIST
I 1178.00 NIST
I 1181.00 NIST
I 1174.00 NIST
I 1171.00 NIST
I 1192.00 NIST
I 1180.00 NIST
I 1181.00 NIST
I Outlier 1155.00 NIST
I 1182.00 NIST
I 1182.00 NIST
I 1182.00 NIST
I 1187.00 NIST
I Outlier 1225.00 NIST
I 1172.00 NIST
I 1175.00 NIST
I 1182.00 NIST
I 1163.00 NIST
I 1171.00 NIST
I 1175.00 NIST
I 1171.00 NIST
I 1187.00 NIST
I 1166.00 NIST
I 1191.00 NIST
I 1186.00 NIST
I 1188.00 NIST
I 1165.00 NIST
I Outlier 1232.00 NIST
I 1186.00 NIST
I 1183.00 NIST
I 1183.00 NIST
I Outlier 1232.00 NIST
I 1171.00 NIST
I 1191.00 NIST
I 1180.00 NIST
I 1190.00 NIST
I 1191.00 NIST
gas 353.60 ± 1.30 J/mol×K NIST
liquid [246.02; 248.10] J/mol×K Show Hide
liquid 246.02 J/mol×K NIST
liquid 248.10 J/mol×K NIST
Tboil [417.43; 417.60] K Show Hide
Tboil 417.60 K KDB
Tboil 417.50 K Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
Tboil 417.43 K Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
Tboil 417.55 K Vapor-Liquid Equilibria Data for Binary Systems of Ethylbenzene + Xylene Isomers at 100.65 kPa
Tboil 417.56 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
Tc 630.30 K KDB
Tfus [247.90; 248.08] K Show Hide
Tfus 247.90 K KDB
Tfus 248.08 K Aq. Solubility Prediction
Ttriple 247.80 ± 0.25 K NIST
Vc [0.370; 0.370] m3/kmol Show Hide
Vc 0.370 m3/kmol KDB
Vc 0.370 m3/kmol NIST
Zc 0.2634870 KDB
Zra 0.26 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [168.20; 192.50] J/mol×K [393.00; 463.00] Show Hide
Cp,gas 168.20 ± 1.70 J/mol×K 393.00 NIST
Cp,gas 182.00 ± 1.70 J/mol×K 428.00 NIST
Cp,gas 192.50 ± 2.10 J/mol×K 463.00 NIST
Cp,liquid [182.40; 206.70] J/mol×K [298.00; 347.00] Show Hide
Cp,liquid 187.00 J/mol×K 298.00 NIST
Cp,liquid 183.89 J/mol×K 298.10 NIST
Cp,liquid 187.65 J/mol×K 298.15 NIST
Cp,liquid 187.58 J/mol×K 298.15 NIST
Cp,liquid 187.82 J/mol×K 298.15 NIST
Cp,liquid 182.40 J/mol×K 303.00 NIST
Cp,liquid 206.70 J/mol×K 347.00 NIST
η [0.0004136; 0.0008710] Pa×s [288.15; 353.15] Show Hide
η 0.0008710 Pa×s 288.15 Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η 0.0008092 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 0.0008100 Pa×s 293.15 Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η 0.0007576 Pa×s 298.15 Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η 0.0007610 Pa×s 298.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0007580 Pa×s 298.15 Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η 0.0007560 Pa×s 298.15 Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η 0.0007440 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 0.0007590 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 0.0006950 Pa×s 303.15 Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η 0.0007095 Pa×s 303.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0007100 Pa×s 303.15 Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η 0.0007080 Pa×s 303.15 Viscosities, Densities, and Speeds of Sound of Binary Mixtures of Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene with Anisole at (288.15, 293.15, 298.15, and 303.15) K
η 0.0006950 Pa×s 303.15 Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η 0.0007062 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 0.0007404 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 0.0007172 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 0.0006660 Pa×s 308.15 Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η 0.0006650 Pa×s 308.15 Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η 0.0006690 Pa×s 308.15 Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η 0.0006900 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 0.0006580 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 0.0006660 Pa×s 308.15 Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η 0.0006292 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 0.0006451 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 0.0006210 Pa×s 313.15 Viscosity, Density, and Refractive Index of Some (Ester + Hydrocarbon) Binary Mixtures at 303.15 K and 313.15 K
η 0.0006261 Pa×s 313.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0006210 Pa×s 313.15 Thermophysical Properties of Isoamyl Acetate or Methyl Benzoate + Hydrocarbon Binary Mixtures, at (303.15 and 313.15) K
η 0.0006280 Pa×s 313.15 Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η 0.0005972 Pa×s 318.15 Ultrasonic and viscometric study of molecular interactions in binary mixtures of aniline with 1-propanol, 2-propanol, 2-methyl-1-propanol, and 2-methyl-2-propanol at different temperatures
η 0.0005890 Pa×s 318.15 Densities and Viscosities of Binary Mixtures of Methyl 4-Chlorobutyrate with Aromatic Hydrocarbons at T ) (298.15 to 318.15) K
η 0.0005910 Pa×s 318.15 Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η 0.0006117 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 0.0005910 Pa×s 318.15 Density and Viscosity of the Binary Mixtures of Hexan-1-ol with Isomeric Xylenes at T = (308.15 and 318.15) K and Atmospheric Pressure
η 0.0005554 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 0.0005600 Pa×s 323.15 Viscometric Studies of Molecular Interactions in Binary Liquid Mixtures of Isomeric Xylenes with Methanol
η 0.0005711 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 0.0005584 Pa×s 323.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0005433 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 0.0005105 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 0.0005020 Pa×s 333.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0004544 Pa×s 343.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
η 0.0004136 Pa×s 353.15 Densities and Viscosities of N-Formylmorpholine (NFM) + p-Xylene, + o-Xylene, + m-Xylene at Different Temperatures and Atmospheric Pressure
ΔfusH [13.60; 13.60] kJ/mol [247.80; 247.82] Show Hide
ΔfusH 13.60 kJ/mol 247.80 NIST
ΔfusH 13.60 kJ/mol 247.80 NIST
ΔfusH 13.60 kJ/mol 247.82 NIST
ΔsubH 60.10 kJ/mol 248.00 NIST
ΔvapH [36.24; 45.00] kJ/mol [298.00; 598.50] Show Hide
ΔvapH 43.07 kJ/mol 298.00 Enthalpies of Vaporization and Vapor Pressures of Some Deuterated Hydrocarbons. Liquid-Vapor Pressure Isotope Effects
ΔvapH 45.00 kJ/mol 298.00 NIST
ΔvapH 41.10 kJ/mol 376.00 NIST
ΔvapH 40.80 kJ/mol 378.00 NIST
ΔvapH 39.80 kJ/mol 401.00 NIST
ΔvapH 36.82 kJ/mol 417.50 KDB
ΔvapH 36.24 kJ/mol 417.60 NIST
ΔvapH 38.00 kJ/mol 444.50 NIST
ΔvapH 36.70 kJ/mol 521.00 NIST
ΔvapH 36.70 kJ/mol 598.50 NIST
Pvap [0.88; 250.00] kPa [298.15; 456.10] Show Hide
Pvap 0.88 kPa 298.15 (Vapour + liquid) equilibria of (1-butanol + benzene, or toluene, or o-, or m-, or p-xylene) at T = 308.15 K
Pvap 2.05 kPa 313.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 3.46 kPa 323.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 3.60 kPa 323.15 Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
Pvap 5.44 kPa 333.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 5.61 kPa 333.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 5.32 kPa 333.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 5.45 kPa 333.15 Vapor liquid equilibria and density measurement for binary mixtures of o-xylene + NMF, m-xylene +NMF and p-xylene +NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
Pvap 8.54 kPa 343.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 8.47 kPa 343.15 Vapor liquid equilibria and density measurement for binary mixtures of o-xylene + NMF, m-xylene +NMF and p-xylene +NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
Pvap 9.18 kPa 345.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 11.27 kPa 350.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 12.71 kPa 353.15 Vapor liquid equilibria and density measurement for binary mixtures of o-xylene + NMF, m-xylene +NMF and p-xylene +NMF at 333.15 K, 343.15 K and 353.15 K from 0 kPa to 101.3 kPa
Pvap 12.66 kPa 353.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 12.80 kPa 353.15 Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
Pvap 12.73 kPa 353.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 13.73 kPa 355.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 14.75 kPa 357.30 Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
Pvap 16.62 kPa 360.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 18.65 kPa 363.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 20.00 kPa 365.15 Vapour-liquid equilibrium for tripropylene glycol + aromatic hydrocarbons binary systems: Experimental data and regression
Pvap 20.40 kPa 365.49 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 26.73 kPa 373.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 29.61 kPa 376.70 Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
Pvap 30.14 kPa 376.75 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 31.66 kPa 378.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 37.35 kPa 383.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 40.20 kPa 385.55 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 43.63 kPa 388.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 49.44 kPa 392.70 Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
Pvap 50.43 kPa 392.87 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 50.60 kPa 393.04 Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
Pvap 51.01 kPa 393.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 60.03 kPa 398.66 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 64.27 kPa 401.50 Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
Pvap 68.42 kPa 403.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 70.27 kPa 404.09 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 80.41 kPa 408.83 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 90.54 kPa 413.06 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 90.18 kPa 413.15 Vapor-liquid equilibrium for the binary mixtures of dipropylene glycol with aromatic hydrocarbons: Experimental and regression
Pvap 90.39 kPa 413.15 Vapor-Liquid Equilibrium Data, Excess Enthalpy Data, and Azeotropic Data for the Binary System Dibutyl Ether + o-Xylene
Pvap 93.13 kPa 414.41 Refractive Index and Vapor-Liquid Equilibrium Data for the Binary Systems of Anisole with Xylene Isomers at 93.13 kPa
Pvap 101.85 kPa 417.28 Vapor liquid equilibrium for the binary systems tetrahydrothiophene + toluene and tetrahydrothiophene + o-xylene at 368.15 K and 383.15 K
Pvap 101.30 kPa 417.43 Measurement and Correlation of Vapor-Liquid Equilibrium for Binary Systems of Dimethyl Carbonate with Butyl Butyrate, o-Xylene, and Cyclohexanone at 101.3 kPa
Pvap 102.78 kPa 418.60 Extension of the DSC method to measuring vapor pressures of narrow boiling range oil cuts
Pvap 250.00 kPa 456.10 Isobaric Vapor Liquid Equilibrium for Binary Systems of 2,2,4-Trimethylpentane with o-Xylene, m-Xylene, p-Xylene, and Ethylbenzene at 250 kPa
n0 [1.48580; 1.50830]   [288.15; 318.15] Show Hide
n0 1.50830 288.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.50720 288.15 Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0 1.50830 288.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.50570 293.10 Volumetric properties of (cyclohexanone + a xylene) at temperature between (293.15 and 353.15) K
n0 1.50550 293.15 Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n0 1.50550 293.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.50550 293.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.48580 293.15 Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0 1.50570 293.15 Densities and volumetric properties of a (xylene + dimethyl sulfoxide) at temperature from (293.15 to 353.15) K
n0 1.50573 293.15 A study of densities and volumetric properties of binary mixtures containing nitrobenzene at T = (293.15 to 353.15) K
n0 1.50550 293.15 Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0 1.50470 293.15 Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0 1.50550 293.15 Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
n0 1.50150 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 1.50260 298.00 Vapor-Liquid Equilibrium for Dimethyl Disulfide + Butane, + trans-But-2-ene, + 2-Methylpropane, + 2-Methylpropene, + Ethanol, and 2-Ethoxy-2-methylpropane
n0 1.50570 298.15 Densities and volumetric properties of binary mixtures of xylene with N,N-dimethylformamide at different temperatures
n0 1.50280 298.15 Phase equilibria of binary systems of 3-methylthiophene with four different hydrocarbons
n0 1.50200 298.15 Isobaric Vapor-Liquid Equilibria for the Binary Mixtures of Styrene with Ethylbenzene, o-Xylene, m-Xylene, and p-Xylene
n0 1.50300 298.15 Bubble temperature measurements on the binary mixtures formed by decane with a variety of compounds at 95.8 kPa
n0 1.50180 298.15 Liquid-liquid equilibria for mixtures of (Furfural + an Aromatic hydrocarbon + an alkane) at T=298.15 K
n0 1.50290 298.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.50280 298.15 Phase equilibria on four binary systems containing 3-methylthiophene
n0 1.50240 298.15 Densities, Excess Molar Volumes, Viscosity, and Refractive Indices of Binary Mixtures of Ethanoic Acid and Trichloroethylene with Dimethylbenzenes at Different Temperatures
n0 1.50180 298.15 Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0 1.50290 298.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.50260 298.15 Vapor-Liquid Equilibrium for Binary System of 1-Propanethiol, Thiophene, and Diethyl Sulfide with Toluene at 90.03 kPa
n0 1.50295 298.15 KDB
n0 1.50262 298.15 Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
n0 1.50570 298.15 A study of densities and volumetric properties of binary mixtures of N-methyl-2-pyrrolidone with xylene at different temperatures and atmospheric pressure
n0 1.50020 303.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.50020 303.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.50000 303.15 Excess molar volumes and refractive indices of (methoxybenzene + benzene, or toluene, or o-xylene, or m-xylene, or p-xylene, or mesitylene) binary mixtures between T = (288.15 to 303.15) K
n0 1.49750 308.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.50310 308.15 Topological and thermodynamic investigations of molecular interactions in binary mixtures: Molar excess volumes and molar excess enthalpies
n0 1.49750 308.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49480 313.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49480 313.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
n0 1.49466 313.15 Density, Speed of Sound, and Refractive Index for Binary Mixtures Containing Cycloalkanes with o-Xylene, m-Xylene, p-Xylene, and Mesitylene at T = (298.15 and 313.15) K
n0 1.49210 318.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49210 318.15 Densities, Refractive Indices, and Excess Properties of Binary Mixtures of 1,4-Dioxane with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from (288.15 to 318.15) K
ρl [746.76; 884.09] kg/m3 [288.15; 353.15] Show Hide
ρl 883.91 kg/m3 288.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 884.07 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 884.09 kg/m3 288.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 880.00 kg/m3 293.00 KDB
ρl 879.72 kg/m3 293.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 879.83 kg/m3 293.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 879.68 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 878.60 kg/m3 293.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 875.91 kg/m3 298.15 Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl 875.57 kg/m3 298.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 875.90 kg/m3 298.15 Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
ρl 859.54 kg/m3 298.15 Isobaric vapor-liquid equilibrium of binary systems of decane with p-, o-, m-xylene at 20 kPa
ρl 859.54 kg/m3 298.15 Isobaric vapor-liquid equilibrium data of the binary systems of octane with p, o, m-xylene at 20 kPa
ρl 875.50 kg/m3 298.15 Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
ρl 875.91 kg/m3 298.15 Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl 875.99 kg/m3 298.15 Molar Excess Volumes and Excess Isentropic Compressibilities of Ternary Mixtures of o-Toluidine
ρl 874.89 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 875.90 kg/m3 298.15 Molar Excess Volumes and Excess Isentropic Compressibilities of {2-Methylaniline (i) + Benzene (j) + Methylbenzene}, {2-Methylaniline (i) + Benzene (j) + 1,2-Dimethylbenzene (k)}, and {2-Methylaniline (i) + Benzene (j) + 1,4-Dimethylbenzene (k)} at T = 308.15 K
ρl 875.52 kg/m3 298.15 Evaluation of the Performance of Four Solvents for the Liquid Liquid Extraction of Acrylic Acid from Water
ρl 875.81 kg/m3 298.15 Vapor Liquid Equilibrium for 2-Methyl-1-butanol + Ethylbenzene + Xylene Isomers at 101.33 kPa
ρl 875.72 kg/m3 298.15 Excess Molar Volumes of 2,4,6,8-Tetramethylcyclotetrasiloxane with Benzene, Toluene, and Xylene at T = (288.15, 298.15, and 308.15) K
ρl 875.92 kg/m3 298.15 Excess Molar Volumes and Surface Tensions of Xylene with Isopropyl Ether or Methyl tert-Butyl Ether at 298.15 K
ρl 875.92 kg/m3 298.15 Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
ρl 875.00 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 875.99 kg/m3 298.15 Thermodynamic Properties of Ternary Liquid Mixtures of 2-Pyrrolidinone with Aromatic Hydrocarbons
ρl 875.00 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 875.60 kg/m3 298.15 Volumetric Properties of the D2EHPA-o-Xylene-Neodymium (Samarium, Europium, Gadolinium, Terbium, Dysprosium) Di(2-ethylhexyl)phosphate Systems at 298.15 K
ρl 875.81 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 875.67 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 875.36 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 875.51 kg/m3 298.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 875.50 kg/m3 298.20 Isobaric Vapor Liquid Equilibrium of Binary Systems of Hexane or Octane with 1,2-Dimethylbenzene or 1,3-Dimethylbenzene at 101.3 kPa
ρl 871.70 kg/m3 303.15 Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl 871.70 kg/m3 303.15 Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl 871.30 kg/m3 303.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 872.25 kg/m3 303.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 871.50 kg/m3 303.15 Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl 871.31 kg/m3 303.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 867.48 kg/m3 308.15 Heat capacities of binary and ternary mixtures containing o-chlorotoluene, cyclic ether and aromatic hydrocarbons
ρl 867.48 kg/m3 308.15 Thermodynamic Properties of Ternary Liquid Mixtures Containing o-Chlorotoluene: Excess Molar Volumes and Excess Isentropic Compressibilities
ρl 867.05 kg/m3 308.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 867.20 kg/m3 308.15 Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl 867.07 kg/m3 308.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 866.51 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 867.30 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 862.79 kg/m3 313.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 862.83 kg/m3 313.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 862.80 kg/m3 313.15 Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl 859.67 kg/m3 313.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 858.81 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 858.80 kg/m3 318.15 Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl 858.53 kg/m3 318.15 Densities and Volumetric Properties of Binary Mixtures of Butyl Acrylate with Benzene, Toluene, o-Xylene, m-Xylene, p-Xylene, and Mesitylene at Temperatures from 288.15 K to 318.15 K
ρl 858.57 kg/m3 318.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 840.84 kg/m3 323.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 854.30 kg/m3 323.15 Densities and Dynamic Viscosities of Alicyclic Cyclohexane with Toluene, o-Xylene, and Mesitylene at T = (303.15 to 323.15) K and Atmospheric Pressure
ρl 854.30 kg/m3 323.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 850.24 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 850.01 kg/m3 328.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 815.74 kg/m3 333.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 845.71 kg/m3 333.15 Thermodynamic characterization of binary mixtures of poly(propylene glycol) 425 with toluene and o-, m- and p-xylenes
ρl 784.38 kg/m3 343.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ρl 746.76 kg/m3 353.15 Excess volumes and partial molar volumes of binary mixtures of 1,2-propanediol carbonate with xylene in the temperature range of (293.15 to 353.15) K
ΔfusS 54.87 J/mol×K 247.82 NIST
csound,fluid [1240.87; 1381.29] m/s [288.15; 323.15] Show Hide
csound,fluid 1381.29 m/s 288.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1371.75 m/s 290.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1367.70 m/s 293.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1362.16 m/s 293.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1369.00 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 1351.83 m/s 295.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1341.51 m/s 298.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1346.00 m/s 298.15 Isentropic Compressibilities Changes of Mixing of Tetrahydropyran and Aromatic Hydrocarbons Ternary Mixtures at 308.15 K
csound,fluid 1347.50 m/s 298.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1331.21 m/s 300.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1329.40 m/s 303.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1328.00 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 1320.96 m/s 303.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1310.79 m/s 305.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1300.66 m/s 308.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1313.30 m/s 308.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1290.59 m/s 310.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1298.50 m/s 313.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1280.61 m/s 313.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1289.00 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 1270.55 m/s 315.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1285.20 m/s 318.15 Physicochemical study of intermolecular interactions in 1,4-dioxane + aromatic hydrocarbons binary mixtures at different temperatures by using ultrasonic and viscometric methods
csound,fluid 1260.62 m/s 318.15 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1250.66 m/s 320.65 Influence of temperature on thermodynamics of ethers + xylenes
csound,fluid 1240.87 m/s 323.15 Influence of temperature on thermodynamics of ethers + xylenes
γ [0.02; 0.03] N/m [293.20; 343.15] 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 298.15 Experimental and theoretical surface tension deviations in the binary systems propyl propanoate + o-, m- and p-xylene at 298.15K
γ 0.03 N/m 298.15 Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
γ 0.03 N/m 303.15 Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 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 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 308.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 308.15 Excess thermodynamic functions derived from densities and surface tensions of (p- or o-xylene + ethylene glycol dimethyl ether) between the temperatures (298.15 and 308.15) K
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 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 318.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 323.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.03 N/m 333.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
γ 0.02 N/m 343.15 Surface Tension of o-Xylene + Acetic Acid and m-Xylene + Acetic Acid Binary Mixtures from 303.15 K to 343.15 K
λ [0.12; 0.14] W/m×K [257.75; 329.09] Show Hide
λ 0.14 W/m×K 257.75 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.14 W/m×K 257.96 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.14 W/m×K 258.10 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.07 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.27 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 277.42 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 295.56 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 295.78 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 295.91 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 312.07 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 312.29 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.13 W/m×K 312.44 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 328.72 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 328.94 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λ 0.12 W/m×K 329.09 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Datasets

  1. Viscosity, Pa*s (2)
  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
273.48 100.00 0.0011
273.48 1000.00 0.0011
273.48 5000.00 0.0012
273.48 10000.00 0.0012
273.48 15000.00 0.0013
273.48 20000.00 0.0013
273.48 25000.00 0.0014
273.48 30000.00 0.0014
283.22 100.00 0.0009
283.22 1000.00 0.0010
283.22 5000.00 0.0010
283.21 10000.00 0.0010
283.21 15000.00 0.0011
283.21 20000.00 0.0011
283.21 25000.00 0.0012
283.21 30000.00 0.0012
293.04 100.00 0.0008
293.04 1000.00 0.0008
293.04 5000.00 0.0009
293.04 10000.00 0.0009
293.05 15000.00 0.0009
293.05 20000.00 0.0010
293.05 25000.00 0.0010
293.06 30000.00 0.0010
302.87 100.00 0.0007
302.87 1000.00 0.0007
302.88 5000.00 0.0007
302.88 10000.00 0.0008
302.88 15000.00 0.0008
302.87 20000.00 0.0008
302.87 25000.00 0.0009
302.87 30000.00 0.0009
312.66 100.00 0.0006
312.67 1000.00 0.0006
312.67 5000.00 0.0007
312.66 10000.00 0.0007
312.67 15000.00 0.0007
312.66 20000.00 0.0007
312.66 25000.00 0.0008
312.66 30000.00 0.0008
321.85 100.00 0.0006
321.85 1000.00 0.0006
321.86 5000.00 0.0006
321.85 10000.00 0.0006
321.85 15000.00 0.0006
321.86 20000.00 0.0007
321.86 25000.00 0.0007
321.85 30000.00 0.0007
332.47 100.00 0.0005
332.47 1000.00 0.0005
332.48 5000.00 0.0005
332.48 10000.00 0.0006
332.48 15000.00 0.0006
332.48 20000.00 0.0006
332.48 25000.00 0.0006
332.48 30000.00 0.0007
343.06 100.00 0.0005
343.07 1000.00 0.0005
343.07 5000.00 0.0005
343.07 10000.00 0.0005
343.08 15000.00 0.0005
343.09 20000.00 0.0005
343.08 25000.00 0.0006
343.08 30000.00 0.0006
353.04 100.00 0.0004
353.04 1000.00 0.0004
353.03 5000.00 0.0004
353.02 10000.00 0.0005
353.02 15000.00 0.0005
353.02 20000.00 0.0005
353.02 25000.00 0.0005
353.01 30000.00 0.0005
362.85 100.00 0.0004
362.85 1000.00 0.0004
362.85 5000.00 0.0004
362.85 10000.00 0.0004
362.86 15000.00 0.0004
362.86 20000.00 0.0005
362.87 25000.00 0.0005
362.87 30000.00 0.0005
372.83 100.00 0.0004
372.84 1000.00 0.0004
372.84 5000.00 0.0004
372.85 10000.00 0.0004
372.86 15000.00 0.0004
372.86 20000.00 0.0004
372.85 25000.00 0.0004
372.86 30000.00 0.0004
Reference
Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Viscosity, Pa*s - Liquid
303.15 101.30 0.0007
Reference

Refractive index (Na D-line)

Fixed Measured
Pressure, kPa - Liquid Temperature, K - Liquid Refractive index (Na D-line) - Liquid
93.00 298.15 1.5022
Reference

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
283.15 100.00 890.5
283.15 1000.00 890.8
283.15 3000.00 892.4
283.15 5000.00 893.5
283.15 10000.00 896.7
283.15 15000.00 899.0
283.15 20000.00 902.6
283.15 25000.00 905.3
283.15 30000.00 908.1
283.15 35000.00 910.9
283.15 40000.00 913.3
283.15 50000.00 918.2
283.15 60000.00 923.0
293.15 100.00 879.7
293.15 1000.00 879.9
293.15 3000.00 881.4
293.15 5000.00 882.4
293.15 10000.00 885.9
293.15 15000.00 888.9
293.15 20000.00 892.0
293.15 25000.00 894.9
293.15 30000.00 897.8
293.15 35000.00 900.5
293.15 40000.00 903.1
293.15 50000.00 908.5
293.15 60000.00 913.1
303.15 100.00 870.9
303.15 1000.00 871.6
303.15 3000.00 873.0
303.15 5000.00 874.4
303.15 10000.00 877.8
303.15 15000.00 881.1
303.15 20000.00 884.2
303.15 25000.00 887.3
303.15 30000.00 890.3
303.15 35000.00 893.1
303.15 40000.00 895.9
303.15 50000.00 901.2
303.15 60000.00 906.4
313.15 100.00 862.7
313.15 1000.00 862.9
313.15 3000.00 864.5
313.15 5000.00 865.9
313.15 10000.00 869.6
313.15 15000.00 873.0
313.15 20000.00 876.3
313.15 25000.00 879.6
313.15 30000.00 882.7
313.15 35000.00 885.7
313.15 40000.00 888.4
313.15 50000.00 894.2
313.15 60000.00 899.2
323.15 100.00 853.8
323.15 1000.00 854.6
323.15 3000.00 856.1
323.15 5000.00 857.7
323.15 10000.00 861.5
323.15 15000.00 865.2
323.15 20000.00 868.8
323.15 25000.00 872.0
323.15 30000.00 875.3
323.15 35000.00 878.4
323.15 40000.00 881.5
323.15 50000.00 887.3
323.15 60000.00 892.8
333.15 100.00 845.1
333.15 1000.00 846.0
333.15 3000.00 847.8
333.15 5000.00 849.4
333.15 10000.00 853.3
333.15 15000.00 857.1
333.15 20000.00 860.9
333.15 25000.00 864.4
333.15 30000.00 867.8
333.15 35000.00 871.0
333.15 40000.00 874.3
333.15 50000.00 880.3
333.15 60000.00 886.0
343.15 100.00 836.3
343.15 1000.00 837.2
343.15 3000.00 839.0
343.15 5000.00 840.9
343.15 10000.00 844.9
343.15 15000.00 849.0
343.15 20000.00 853.0
343.15 25000.00 856.6
343.15 30000.00 860.2
343.15 35000.00 863.7
343.15 40000.00 866.8
343.15 50000.00 873.2
343.15 60000.00 878.9
353.15 100.00 827.8
353.15 1000.00 828.6
353.15 3000.00 830.6
353.15 5000.00 832.4
353.15 10000.00 836.9
353.15 15000.00 841.2
353.15 20000.00 845.1
353.15 25000.00 849.1
353.15 30000.00 852.8
353.15 35000.00 856.4
353.15 40000.00 859.8
353.15 50000.00 866.3
353.15 60000.00 872.5
363.15 100.00 819.3
363.15 1000.00 820.3
363.15 3000.00 822.4
363.15 5000.00 824.3
363.15 10000.00 828.7
363.15 15000.00 833.6
363.15 20000.00 837.6
363.15 25000.00 841.5
363.15 30000.00 845.5
363.15 35000.00 849.3
363.15 40000.00 853.1
363.15 50000.00 859.8
363.15 60000.00 866.3
Reference

Correlations

Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [305.32; 445.43] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Pvp) = A + B/(T + C)
Coefficient A1.44465e+01
Coefficient B-3.60720e+03
Coefficient C-5.05540e+01
Temperature range, min.305.32
Temperature range, max.445.43
Pvap 1.33 kPa 305.32 Calculated Property
Pvap 3.01 kPa 320.89 Calculated Property
Pvap 6.23 kPa 336.46 Calculated Property
Pvap 11.95 kPa 352.02 Calculated Property
Pvap 21.51 kPa 367.59 Calculated Property
Pvap 36.64 kPa 383.16 Calculated Property
Pvap 59.51 kPa 398.73 Calculated Property
Pvap 92.72 kPa 414.29 Calculated Property
Pvap 139.29 kPa 429.86 Calculated Property
Pvap 202.65 kPa 445.43 Calculated Property
Pvap [0.02; 3724.86] kPa [247.98; 630.37] KDB Vapor Pressure Data Show Hide
Equationln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A8.33218e+01
Coefficient B-7.94623e+03
Coefficient C-1.00606e+01
Coefficient D5.93974e-06
Temperature range, min.247.98
Temperature range, max.630.37
Pvap 0.02 kPa 247.98 Calculated Property
Pvap 0.55 kPa 290.47 Calculated Property
Pvap 5.38 kPa 332.96 Calculated Property
Pvap 28.61 kPa 375.44 Calculated Property
Pvap 102.23 kPa 417.93 Calculated Property
Pvap 278.49 kPa 460.42 Calculated Property
Pvap 628.00 kPa 502.91 Calculated Property
Pvap 1238.99 kPa 545.39 Calculated Property
Pvap 2222.36 kPa 587.88 Calculated Property
Pvap 3724.86 kPa 630.37 Calculated Property

Similar Compounds

2-Methylbenzyl radical. 1,2-Di(methyl-d3)benzene-d4. Benzene, 1,2,3-trimethyl-. Benzene, 1,2,4-trimethyl-. Benzene, 1,2,3,4-tetramethyl-. Benzonitrile, 2-methyl-. 3-Methylbenzyl radical. Benzene, 1,3-dimethyl-. Toluene. Toluene-D3. Toluene-D8. Benzene, 1,2,3,5-tetramethyl-. 2-Methylphenylacetylene. Benzaldehyde, 2-methyl-. Benzonitrile, 3,4-dimethyl-.

Find more compounds similar to o-Xylene.

Mixtures

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Sources

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