Chemical Properties of Mesitylene (CAS 108-67-8)

Mesitylene

InChI
InChI=1S/C9H12/c1-7-4-8(2)6-9(3)5-7/h4-6H,1-3H3
InChI Key
AUHZEENZYGFFBQ-UHFFFAOYSA-N
Formula
C9H12
SMILES
Cc1cc(C)cc(C)c1
Molecular Weight1
120.19
CAS
108-67-8
Other Names
  • 1,3,5-trimethylbenzene
  • 1,3,5-trimethylbenzene (mesitylene)
  • 2,4,6-Trimethylbenzene
  • 3,5-Dimethyltoluene
  • Benzene, 1,3,5-trimethyl-
  • Fleet-X
  • NSC 9273
  • S-TRIMETHYLBENEZENE
  • TMB
  • UN 2325
  • s-Trimethylbenzene
  • sym-Trimethylbenzene
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Physical Properties

Property Value Unit Source
ω [0.3796; 0.3990]   Show Hide
ω 0.3796 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.3980 Passut and Danner (1973), critical constants and acentric factors Compiled value
ω 0.3990 ChemSep v8.3 pure component data Compiled value
ω 0.3990 KDB
PAff [835.10; 836.20] kJ/mol Show Hide
PAff 836.20 kJ/mol NIST
PAff 835.10 kJ/mol NIST
BasG [808.60; 808.80] kJ/mol Show Hide
BasG 808.60 kJ/mol NIST
BasG 808.80 kJ/mol NIST
ΔcH°liquid [-5202.70; -5193.10] kJ/mol Show Hide
ΔcH°liquid -5193.10 ± 1.30 kJ/mol NIST
ΔcH°liquid -5202.70 kJ/mol NIST
Cp,liquid 207.43 J/mol×K Thermodynamics of mixtures involving some (benzene derivatives + benzonitrile)
μ [0.00; 0.10] debye Show Hide
μ 0.00 debye ChemSep v8.3 pure component data Compiled value
μ 0.10 debye KDB
ΔfG° [118.00; 118.10] kJ/mol Show Hide
ΔfG° 118.10 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° 118.00 kJ/mol KDB
Δc,grossH 5193.14 kJ/mol KDB
Δc,netH 4929.045 kJ/mol KDB
ΔfH°gas [-16.08; -16.05] kJ/mol Show Hide
ΔfH°gas -16.05 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -16.08 kJ/mol KDB
ΔfusH° 12.33 kJ/mol Joback Calculated Property
ΔvapH° [47.47; 47.60] kJ/mol Show Hide
ΔvapH° 47.51 kJ/mol NIST
ΔvapH° Outlier 47.60 kJ/mol NIST
ΔvapH° 47.50 ± 2.10 kJ/mol NIST
ΔvapH° 47.50 ± 0.10 kJ/mol NIST
ΔvapH° 47.50 kJ/mol NIST
ΔvapH° 47.50 ± 0.20 kJ/mol NIST
ΔvapH° 47.50 kJ/mol NIST
ΔvapH° 47.47 kJ/mol NIST
IE [8.20; 8.65] eV Show Hide
IE 8.40 ± 0.01 eV NIST
IE 8.41 ± 0.01 eV NIST
IE 8.46 eV NIST
IE Outlier 8.20 ± 0.10 eV NIST
IE 8.47 eV NIST
IE 8.40 ± 0.01 eV NIST
IE 8.55 eV NIST
IE 8.39 ± 0.01 eV NIST
IE 8.41 ± 0.02 eV NIST
IE 8.42 eV NIST
IE 8.42 eV NIST
IE 8.45 eV NIST
IE 8.45 ± 0.05 eV NIST
IE 8.45 ± 0.05 eV NIST
IE Outlier 8.65 ± 0.03 eV NIST
log10WS [-3.40; -3.40]   Show Hide
log10WS -3.40 Aq. Solubility Prediction
log10WS -3.40 Estimated Solubility
logPoct/wat 2.612 Crippen Calculated Property
McVol 113.910 ml/mol McGowan Calculated Property
Pc [3126.77; 3260.00] kPa Show Hide
Pc 3127.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Pc 3130.94 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 3126.77 kPa Passut and Danner (1973), critical constants and acentric factors Compiled value
Pc 3127.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 3127.00 kPa KDB
Pc 3130.00 ± 40.00 kPa NIST
Pc 3161.90 ± 0.31 kPa NIST
Pc 3255.00 ± 0.32 kPa NIST
Pc 3127.00 ± 6.00 kPa NIST
Pc Outlier 3260.00 ± 9.81 kPa NIST
Ptriple 7.42e-04 kPa ChemSep v8.3 pure component data Compiled value
Inp [152.10; 1013.00]   Show Hide
Inp 979.50 NIST
Inp 984.80 NIST
Inp 947.50 NIST
Inp 952.20 NIST
Inp 953.33 NIST
Inp 963.80 NIST
Inp 972.10 NIST
Inp 976.10 NIST
Inp 981.30 NIST
Inp 969.00 NIST
Inp 952.00 NIST
Inp 952.00 NIST
Inp 962.00 NIST
Inp 962.00 NIST
Inp 962.40 NIST
Inp 967.30 NIST
Inp 969.00 NIST
Inp 963.00 NIST
Inp 962.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 968.00 NIST
Inp 975.00 NIST
Inp 968.00 NIST
Inp 966.00 NIST
Inp 952.70 NIST
Inp 953.10 NIST
Inp 956.20 NIST
Inp 972.00 NIST
Inp 960.00 NIST
Inp 963.00 NIST
Inp 968.00 NIST
Inp 974.00 NIST
Inp 965.00 NIST
Inp 967.10 NIST
Inp 963.30 NIST
Inp 967.90 NIST
Inp 973.50 NIST
Inp 957.00 NIST
Inp 972.00 NIST
Inp 964.70 NIST
Inp 965.00 NIST
Inp 965.40 NIST
Inp 964.60 NIST
Inp 965.00 NIST
Inp 965.00 NIST
Inp 967.10 NIST
Inp 969.00 NIST
Inp 965.50 NIST
Inp 965.50 NIST
Inp 962.70 NIST
Inp 988.00 NIST
Inp 1000.00 NIST
Inp 990.00 NIST
Inp 1000.00 NIST
Inp 1000.00 NIST
Inp 986.00 NIST
Inp 967.00 NIST
Inp 952.10 NIST
Inp 967.60 NIST
Inp 971.00 NIST
Inp 964.00 NIST
Inp 971.20 NIST
Inp 965.30 NIST
Inp 1001.00 NIST
Inp 1001.00 NIST
Inp 1007.00 NIST
Inp 1013.00 NIST
Inp 998.00 NIST
Inp 968.00 NIST
Inp 974.00 NIST
Inp 995.00 NIST
Inp 1002.00 NIST
Inp 996.40 NIST
Inp 955.00 NIST
Inp 970.10 NIST
Inp 998.00 NIST
Inp 981.00 NIST
Inp 953.00 NIST
Inp 959.00 NIST
Inp 960.00 NIST
Inp 995.00 NIST
Inp 961.80 NIST
Inp 969.00 NIST
Inp 970.00 NIST
Inp 996.00 NIST
Inp 1002.00 NIST
Inp 996.00 NIST
Inp 956.00 NIST
Inp 962.00 NIST
Inp 996.00 NIST
Inp 1006.00 NIST
Inp 975.00 NIST
Inp 959.90 NIST
Inp 996.00 NIST
Inp 961.50 NIST
Inp 964.90 NIST
Inp 967.10 NIST
Inp 948.90 NIST
Inp 974.20 NIST
Inp 996.00 NIST
Inp 994.00 NIST
Inp 954.50 NIST
Inp 958.00 NIST
Inp 984.30 NIST
Inp 958.00 NIST
Inp 964.10 NIST
Inp 955.50 NIST
Inp 961.50 NIST
Inp 964.90 NIST
Inp 967.10 NIST
Inp 954.28 NIST
Inp 954.69 NIST
Inp 955.00 NIST
Inp 963.00 NIST
Inp 954.56 NIST
Inp 956.80 NIST
Inp 953.66 NIST
Inp 953.27 NIST
Inp 953.00 NIST
Inp 953.37 NIST
Inp 953.00 NIST
Inp 997.20 NIST
Inp 978.22 NIST
Inp 956.00 NIST
Inp 985.00 NIST
Inp 963.00 NIST
Inp 967.00 NIST
Inp 968.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 967.00 NIST
Inp 967.00 NIST
Inp 954.00 NIST
Inp 967.00 NIST
Inp 972.00 NIST
Inp 958.00 NIST
Inp 972.00 NIST
Inp 968.00 NIST
Inp 961.00 NIST
Inp 965.00 NIST
Inp 956.00 NIST
Inp 969.00 NIST
Inp 972.00 NIST
Inp 1001.00 NIST
Inp 961.00 NIST
Inp 996.00 NIST
Inp 996.00 NIST
Inp 992.00 NIST
Inp 989.00 NIST
Inp 1001.00 NIST
Inp 1001.00 NIST
Inp 996.00 NIST
Inp 979.00 NIST
Inp 979.00 NIST
Inp 960.00 NIST
Inp 989.00 NIST
Inp 974.00 NIST
Inp 1003.00 NIST
Inp 985.00 NIST
Inp 988.00 NIST
Inp 952.00 NIST
Inp 971.00 NIST
Inp 964.00 NIST
Inp 994.00 NIST
Inp 994.00 NIST
Inp 994.00 NIST
Inp 995.00 NIST
Inp 963.00 NIST
Inp 956.18 NIST
Inp 958.00 NIST
Inp 954.00 NIST
Inp 957.00 NIST
Inp 974.70 NIST
Inp 962.00 NIST
Inp 952.00 NIST
Inp 956.00 NIST
Inp 956.00 NIST
Inp 940.00 NIST
Inp 960.00 NIST
Inp 963.00 NIST
Inp 995.00 NIST
Inp 996.00 NIST
Inp 999.00 NIST
Inp 996.00 NIST
Inp 995.00 NIST
Inp 994.00 NIST
Inp 994.00 NIST
Inp 992.00 NIST
Inp 996.00 NIST
Inp 997.00 NIST
Inp 964.00 NIST
Inp 964.00 NIST
Inp 956.00 NIST
Inp 963.00 NIST
Inp 953.00 NIST
Inp 1003.00 NIST
Inp 962.00 NIST
Inp 963.00 NIST
Inp 963.00 NIST
Inp 985.00 NIST
Inp 956.00 NIST
Inp 964.00 NIST
Inp 954.00 NIST
Inp 969.00 NIST
Inp 954.00 NIST
Inp 962.60 NIST
Inp 968.90 NIST
Inp 966.50 NIST
Inp 967.40 NIST
Inp 967.70 NIST
Inp 976.00 NIST
Inp 952.00 NIST
Inp 953.00 NIST
Inp 954.00 NIST
Inp 960.00 NIST
Inp 973.00 NIST
Inp 968.00 NIST
Inp 973.00 NIST
Inp 968.00 NIST
Inp Outlier 173.80 NIST
Inp Outlier 152.10 NIST
Inp 961.80 NIST
Inp 996.00 NIST
Inp 961.50 NIST
Inp 958.00 NIST
Inp 967.10 NIST
Inp 954.56 NIST
Inp 953.37 NIST
Inp 963.00 NIST
Inp 995.00 NIST
Inp 997.00 NIST
Inp 953.00 NIST
Inp 985.00 NIST
Inp 954.00 NIST
Inp 967.70 NIST
Inp 960.00 NIST
Ip [1210.00; 1300.70]   Show Hide
Ip 1275.10 NIST
Ip 1287.30 NIST
Ip Outlier 1300.70 NIST
Ip 1217.00 NIST
Ip 1220.00 NIST
Ip 1242.20 NIST
Ip 1236.90 NIST
Ip 1220.30 NIST
Ip 1251.00 NIST
Ip 1297.00 NIST
Ip 1210.00 NIST
Ip 1263.00 NIST
Ip 1271.00 NIST
Ip 1279.00 NIST
Ip 1255.00 NIST
Ip 1237.00 NIST
Ip 1254.00 NIST
Ip 1268.30 NIST
Ip 1237.00 NIST
Ip 1252.00 NIST
Ip 1248.00 NIST
Ip 1283.00 NIST
Ip 1250.00 NIST
Ip 1241.00 NIST
Ip 1246.00 NIST
Ip 1249.00 NIST
Ip 1221.00 NIST
Ip 1221.00 NIST
Ip 1251.00 NIST
Ip 1253.00 NIST
Ip 1248.00 NIST
Ip 1249.00 NIST
Ip 1254.00 NIST
Ip 1257.00 NIST
Ip 1270.00 NIST
Ip 1281.00 NIST
Ip 1297.00 NIST
Ip 1233.00 NIST
Ip 1245.00 NIST
Ip 1220.00 NIST
Ip 1246.00 NIST
Ip 1287.00 NIST
Ip 1290.00 NIST
Ip 1288.00 NIST
Ip 1242.00 NIST
Ip 1291.00 NIST
Ip 1251.00 NIST
Ip 1254.00 NIST
Ip 1240.00 NIST
Ip 1251.00 NIST
Ip 1229.00 NIST
Ip 1242.00 NIST
Ip 1220.00 NIST
Ip 1271.00 NIST
Ip 1242.00 NIST
Ip 1271.00 NIST
Ip 1228.00 NIST
Ip 1237.00 NIST
Ip 1248.00 NIST
Ip 1249.00 NIST
S°gas 385.30 ± 0.63 J/mol×K NIST
S°liquid 273.55 J/mol×K NIST
Tboil [431.00; 489.07] K Show Hide
Tboil 437.83 K Phase equilibria of three binary systems containing 2,5-dimethylthiophene and 2-ethylthiophene in hydrocarbons
Tboil 437.90 K ChemSep v8.3 pure component data Compiled value
Tboil 437.89 K KDB
Tboil 437.90 K NIST
Tboil 437.10 ± 1.00 K NIST
Tboil 438.00 ± 3.00 K NIST
Tboil 437.80 ± 1.00 K NIST
Tboil 437.75 ± 1.00 K NIST
Tboil 437.00 ± 1.50 K NIST
Tboil 438.00 ± 4.00 K NIST
Tboil 436.00 ± 4.00 K NIST
Tboil 431.00 ± 5.00 K NIST
Tboil 433.00 ± 5.00 K NIST
Tboil 437.90 ± 0.60 K NIST
Tboil 437.00 ± 4.00 K NIST
Tboil 438.20 ± 0.50 K NIST
Tboil 438.00 ± 0.60 K NIST
Tboil 437.86 ± 0.03 K NIST
Tboil 437.86 ± 0.10 K NIST
Tboil 437.85 ± 0.30 K NIST
Tboil 437.86 ± 0.10 K NIST
Tboil 437.80 ± 0.60 K NIST
Tboil 437.87 ± 0.20 K NIST
Tboil 437.86 ± 0.20 K NIST
Tboil Outlier 489.07 ± 0.25 K NIST
Tboil 438.00 ± 0.30 K NIST
Tboil 438.20 ± 0.50 K NIST
Tboil 437.86 ± 0.20 K NIST
Tboil 438.10 ± 0.60 K NIST
Tboil 437.86 ± 0.20 K NIST
Tboil 437.85 ± 0.20 K NIST
Tboil 437.95 ± 0.30 K NIST
Tboil 437.95 ± 0.30 K NIST
Tboil 437.75 ± 0.25 K NIST
Tboil 438.20 ± 0.50 K NIST
Tboil 437.70 ± 0.50 K NIST
Tboil 436.00 ± 3.00 K NIST
Tboil 438.90 ± 1.50 K NIST
Tboil 437.00 ± 2.00 K NIST
Tboil 437.91 ± 0.30 K NIST
Tboil 438.70 ± 0.30 K NIST
Tboil 437.20 ± 1.50 K NIST
Tboil 437.79 ± 0.25 K NIST
Tboil 437.80 ± 1.00 K NIST
Tboil 437.20 ± 1.50 K NIST
Tboil 437.90 ± 1.00 K NIST
Tboil 437.80 ± 0.50 K NIST
Tboil 437.80 ± 0.50 K NIST
Tboil 437.80 ± 0.50 K NIST
Tboil 437.75 ± 0.30 K NIST
Tboil 439.00 ± 3.00 K NIST
Tboil 438.00 ± 0.30 K NIST
Tboil 438.00 ± 4.00 K NIST
Tboil 437.87 ± 0.30 K NIST
Tboil 437.25 ± 0.50 K NIST
Tboil 435.00 ± 2.00 K NIST
Tboil 438.00 ± 2.00 K NIST
Tc [637.10; 643.70] K Show Hide
Tc 637.30 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 3 Compiled value
Tc 637.30 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 637.36 K Passut and Danner (1973), critical constants and acentric factors Compiled value
Tc 637.30 K ChemSep v8.3 pure component data Compiled value
Tc 637.30 K KDB
Tc 637.30 ± 0.50 K NIST
Tc 638.65 ± 0.06 K NIST
Tc 638.35 ± 0.06 K NIST
Tc 637.10 ± 0.63 K NIST
Tc 637.27 ± 0.10 K NIST
Tc 637.29 ± 0.30 K NIST
Tc Outlier 643.70 ± 6.00 K NIST
Tc 640.90 ± 4.00 K NIST
Tfus [206.67; 228.46] K Show Hide
Tfus 228.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 228.46 K ChemSep v8.3 pure component data Compiled value
Tfus 228.40 K KDB
Tfus 228.23 K Aq. Solubility Prediction
Tfus 223.33 ± 0.10 K NIST
Tfus 221.41 ± 0.10 K NIST
Tfus 228.42 ± 0.07 K NIST
Tfus 228.00 ± 2.00 K NIST
Tfus 219.20 ± 2.00 K NIST
Tfus 227.99 ± 0.30 K NIST
Tfus 228.37 ± 0.30 K NIST
Tfus Outlier 206.67 ± 0.20 K NIST
Tfus 228.41 ± 0.40 K NIST
Tfus 228.42 ± 0.20 K NIST
Tfus 228.31 ± 0.40 K NIST
Tfus 228.41 ± 0.05 K NIST
Tfus 228.43 ± 0.02 K NIST
Tfus 221.47 ± 0.03 K NIST
Tfus 223.36 ± 0.03 K NIST
Tfus 228.36 ± 0.20 K NIST
Tfus 221.45 ± 2.00 K NIST
Tfus 228.35 ± 1.50 K NIST
Tfus 220.45 ± 0.30 K NIST
Tfus 219.70 ± 0.80 K NIST
Tfus 218.70 ± 5.00 K NIST
Tfus 215.70 ± 5.00 K NIST
Ttriple [228.42; 228.42] K Show Hide
Ttriple 228.42 K ChemSep v8.3 pure component data Compiled value
Ttriple 228.42 ± 0.01 K NIST
Ttriple 228.42 ± 0.01 K NIST
UQi 4.10 ChemSep v8.3 pure component data Compiled value
URi 5.39 ChemSep v8.3 pure component data Compiled value
Vc [0.430; 0.433] m3/kmol Show Hide
Vc 0.433 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.430 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2520000 ChemSep v8.3 pure component data Compiled value
Zra 0.25 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [185.20; 259.20] J/mol×K [230.00; 420.00] Show Hide
Cp,liquid 185.20 J/mol×K 230.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 188.60 J/mol×K 240.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 192.00 J/mol×K 250.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 195.40 J/mol×K 260.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 198.70 J/mol×K 270.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 199.80 J/mol×K 273.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 202.10 J/mol×K 280.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 205.60 J/mol×K 290.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 205.50 J/mol×K 294.99 NIST
Cp,liquid 211.30 J/mol×K 298.00 NIST
Cp,liquid 206.50 J/mol×K 298.00 NIST
Cp,liquid 213.00 J/mol×K 298.00 NIST
Cp,liquid 208.40 J/mol×K 298.15 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 209.33 J/mol×K 298.15 NIST
Cp,liquid 207.69 J/mol×K 298.15 NIST
Cp,liquid 207.66 J/mol×K 298.15 NIST
Cp,liquid 207.85 J/mol×K 298.15 NIST
Cp,liquid 201.46 J/mol×K 299.80 NIST
Cp,liquid 209.00 J/mol×K 300.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 212.50 J/mol×K 310.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 216.10 J/mol×K 320.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 219.80 J/mol×K 330.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 223.60 J/mol×K 340.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 227.50 J/mol×K 350.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 231.50 J/mol×K 360.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 235.70 J/mol×K 370.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 240.00 J/mol×K 380.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 244.50 J/mol×K 390.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 249.20 J/mol×K 400.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 254.10 J/mol×K 410.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
Cp,liquid 259.20 J/mol×K 420.00 Zabransky, M., Ruzicka, V., Majer, V. and Domalski, E. (1997), Heat Capacity of Liquids: Critical Review and Recommended Values - Monograph No. 6, J. Phys. & Chem. Ref. Data (JPCRD), National Institute of Standards and Technology, Gaithersburg, MD
η [0.0003400; 0.0008500] Pa×s [278.15; 350.15] Show Hide
η 0.0008500 Pa×s 278.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0008000 Pa×s 284.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0007540 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 0.0007500 Pa×s 290.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0007050 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 0.0006300 Pa×s 296.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0006610 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 0.0006572 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 0.0005700 Pa×s 302.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0006210 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 0.0005300 Pa×s 308.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0005792 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 0.0004900 Pa×s 314.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0005066 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 0.0004600 Pa×s 320.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0004400 Pa×s 325.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0004100 Pa×s 330.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0004000 Pa×s 335.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0003900 Pa×s 340.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0003500 Pa×s 345.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
η 0.0003400 Pa×s 350.15 Shear Viscosity of Mixtures of r-Tocopherol with Nonpolar Solvents
ΔfusH [9.51; 9.51] kJ/mol [228.40; 228.40] Show Hide
ΔfusH 9.51 kJ/mol 228.40 NIST
ΔfusH 9.51 kJ/mol 228.40 NIST
ΔvapH [43.50; 51.10] kJ/mol [261.50; 399.50] Show Hide
ΔvapH 51.10 kJ/mol 261.50 NIST
ΔvapH 47.70 kJ/mol 286.00 NIST
ΔvapH 49.70 kJ/mol 302.50 NIST
ΔvapH 46.20 ± 1.30 kJ/mol 319.00 NIST
ΔvapH 43.50 kJ/mol 386.00 NIST
ΔvapH 43.90 kJ/mol 399.50 NIST
Pvap 101.33 kPa 437.83 Phase equilibria of three binary systems containing 2,5-dimethylthiophene and 2-ethylthiophene in hydrocarbons
n0 [1.48680; 1.50450]   [288.15; 318.15] Show Hide
n0 1.50200 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 1.50450 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 1.50200 288.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49920 293.10 Liquid-Liquid Equilibria Measurements for Ternary System of Hexadecane + 1,3,5-Trimethylbenzene + N-Methyl-2-pyrrolidone
n0 1.49950 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 1.49950 293.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49930 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 1.49684 298.15 KDB
n0 1.49693 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 1.49690 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 1.49760 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 1.49600 298.15 Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0 1.49670 298.15 Excess molar volumes of (octane + benzene, or toluene, or 1,3-xylene, or 1,3,5-trimethylbenzene) at temperatures between (298.15 and 328.15) K
n0 1.48980 298.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.49580 298.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.49690 298.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49682 298.15 Effect of Temperature on the Change of Refractive Index on Mixing for Butyl Acetate + Aromatic Hydrocarbons
n0 1.49480 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 1.49280 303.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.49360 303.15 Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0 1.49440 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 1.49440 303.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.49180 308.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.48980 308.15 Thermodynamic properties of (tetradecane + benzene, + toluene, + chlorobenzene, + bromobenzene, + anisole) binary mixtures at T = (298.15, 303.15, and 308.15) K
n0 1.49180 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 1.49130 308.15 Excess and deviation properties for the binary mixtures of methylcyclohexane with benzene, toluene, p-xylene, mesitylene, and anisole at T = (298.15, 303.15, and 308.15) K
n0 1.48930 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 1.48923 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 1.48930 313.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.48680 318.15 Refractive Indices of Binary Mixtures of Tetrahydrofuran with Aromatic Hydrocarbon at Temperatures from (288.15 to 318.15) K
n0 1.48680 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 [818.50; 869.28] kg/m3 [288.15; 343.15] Show Hide
ρl 869.28 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 865.00 kg/m3 293.00 KDB
ρl 865.37 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 865.10 kg/m3 293.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 861.45 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 860.86 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 861.03 kg/m3 298.15 Excess Molar volumes and Surface Tensions of Trimethylbenzene with Tetrahydrofuran Tetrachloromethane and Dimethylsulfoxide at 298.15 K
ρl 861.03 kg/m3 298.15 Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with 1-Butanol, 2-Methyl-1-propanol, 2-Butanol, and 2-Methyl-2-propanol at 298.15 K
ρl 864.00 kg/m3 298.20 Phase Equilibrium Measurement and Thermodynamic Modeling of the 4-Methylpentan-2-one/3-Methylphenol, and 4-Methylphenol/Water Ternary Systems at 298.2, 313.2, and 323.2 K and 0.1 MPa
ρl 859.70 kg/m3 298.20 Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
ρl 856.90 kg/m3 303.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 857.54 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 857.40 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 852.66 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 853.63 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 853.30 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 842.80 kg/m3 313.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 849.30 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 849.71 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 845.80 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 845.10 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 840.90 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 834.70 kg/m3 323.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 826.60 kg/m3 333.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
ρl 818.50 kg/m3 343.15 Densities and volumetric properties of (N-acetylmorpholine + aromatic hydrocarbon) binary mixtures from T = (293.15 to 343.15) K
csound,fluid [1263.00; 1360.40] m/s [293.15; 318.15] Show Hide
csound,fluid 1360.40 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 1339.80 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 1319.60 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 1300.20 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 1280.40 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 1263.00 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
γ [0.03; 0.03] N/m [298.15; 313.15] Show Hide
γ 0.03 N/m 298.15 Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
γ 0.03 N/m 298.15 Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
γ 0.03 N/m 298.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.03 N/m 298.15 Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ 0.03 N/m 298.15 Excess Molar Volumes and Surface Tensions of 1,2,4- Trimethylbenzene and 1,3,5- Trimethylbenzene with 1,1-Diethoxyethane and 2,2-Dimethoxypropane at (298.15, 308.15, and 313.15) K
γ 0.03 N/m 303.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.03 N/m 308.15 Excess Molar Volumes and Surface Tensions of 1,2,4- Trimethylbenzene and 1,3,5- Trimethylbenzene with 1,1-Diethoxyethane and 2,2-Dimethoxypropane at (298.15, 308.15, and 313.15) K
γ 0.03 N/m 308.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.03 N/m 308.15 Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
γ 0.03 N/m 313.15 Densities and Surface Tensions of Trimethylbenzene + Dimethyl Carbonate or + Diethyl Carbonate at 298.15 K and 313.15 K
γ 0.03 N/m 313.15 Excess Molar Volumes and Surface Tensions of Trimethylbenzene + Ethylene Glycol Ester at 298.15 K and 313.15 K
γ 0.03 N/m 313.15 Densities, surface tensions, and derived surface thermodynamics properties of (trimethylbenzene + propyl acetate, or butyl acetate) from T = 298.15 K to 313.15 K
γ 0.03 N/m 313.15 Excess Molar Volumes and Surface Tensions of 1,2,4- Trimethylbenzene and 1,3,5- Trimethylbenzene with 1,1-Diethoxyethane and 2,2-Dimethoxypropane at (298.15, 308.15, and 313.15) K
γ 0.03 N/m 313.15 Excess Molar Volumes and Surface Tensions of 1,2,4-Trimethylbenzene and 1,3,5-Trimethylbenzene with Isopropyl Acetate and Isobutyl Acetate at (298.15, 308.15, and 313.15) K
λliquid [0.13; 0.14] W/m×K [258.66; 332.28] Show Hide
λliquid 0.14 W/m×K 258.66 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 258.83 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 258.95 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 276.88 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 277.04 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 277.16 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 296.36 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 296.53 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.14 W/m×K 296.66 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 313.44 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 313.60 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 313.73 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 331.99 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 332.16 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons
λliquid 0.13 W/m×K 332.28 Thermal Conductivity and Thermal Diffusivity of Twenty-Nine Liquids: Alkenes, Cyclic (Alkanes, Alkenes, Alkadienes, Aromatics), and Deuterated Hydrocarbons

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [87.72; 417.55] J/mol×K [150.00; 1500.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,gas in J/mol×K, T in K
Coefficient A7.67990e+01
Coefficient B-5.61490e+02
Coefficient C6.10824e+00
Coefficient D1.84880e-04
Coefficient E-8.00410e-08
Temperature range, min.150.00
Temperature range, max.1500.00
Cp,gas 87.72 J/mol×K 150.00 Calculated Property
Cp,gas 149.39 J/mol×K 300.00 Calculated Property
Cp,gas 214.83 J/mol×K 450.00 Calculated Property
Cp,gas 268.23 J/mol×K 600.00 Calculated Property
Cp,gas 310.31 J/mol×K 750.00 Calculated Property
Cp,gas 343.45 J/mol×K 900.00 Calculated Property
Cp,gas 369.56 J/mol×K 1050.00 Calculated Property
Cp,gas 390.03 J/mol×K 1200.00 Calculated Property
Cp,gas 405.79 J/mol×K 1350.00 Calculated Property
Cp,gas 417.55 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [185.39; 230.74] J/mol×K [228.42; 350.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is Cp,liquid in J/mol×K, T in K
Coefficient A1.52130e+02
Coefficient B2.79490e+02
Coefficient C-2.07736e+00
Coefficient D2.46320e-02
Coefficient E-2.43090e-05
Temperature range, min.228.42
Temperature range, max.350.00
Cp,liquid 185.39 J/mol×K 228.42 Calculated Property
Cp,liquid 189.26 J/mol×K 241.93 Calculated Property
Cp,liquid 193.50 J/mol×K 255.44 Calculated Property
Cp,liquid 198.11 J/mol×K 268.95 Calculated Property
Cp,liquid 203.05 J/mol×K 282.46 Calculated Property
Cp,liquid 208.27 J/mol×K 295.96 Calculated Property
Cp,liquid 213.72 J/mol×K 309.47 Calculated Property
Cp,liquid 219.34 J/mol×K 322.98 Calculated Property
Cp,liquid 225.04 J/mol×K 336.49 Calculated Property
Cp,liquid 230.74 J/mol×K 350.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0032299; 0.0001163] Pa×s [228.42; 550.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is η in Pa×s, T in K
Coefficient A-1.12830e+01
Coefficient B1.43930e+03
Coefficient C-1.57870e-01
Coefficient D1.99340e-06
Coefficient E2.00000e+00
Temperature range, min.228.42
Temperature range, max.550.00
η 0.0032299 Pa×s 228.42 Calculated Property
η 0.0013941 Pa×s 264.15 Calculated Property
η 0.0007432 Pa×s 299.88 Calculated Property
η 0.0004583 Pa×s 335.61 Calculated Property
η 0.0003139 Pa×s 371.34 Calculated Property
η 0.0002327 Pa×s 407.08 Calculated Property
η 0.0001834 Pa×s 442.81 Calculated Property
η 0.0001518 Pa×s 478.54 Calculated Property
η 0.0001307 Pa×s 514.27 Calculated Property
η 0.0001163 Pa×s 550.00 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [51.40; 0.00] kJ/mol [228.42; 637.30] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc
Y is ΔvapH in kJ/mol, T in K
Coefficient A6.92920e+01
Coefficient B1.07060e+00
Coefficient C-1.50940e+00
Coefficient D1.26900e+00
Coefficient E-4.28640e-01
Critical temperature, Tc (K)6.37300e+02
Temperature range, min.228.42
Temperature range, max.637.30
ΔvapH 51.40 kJ/mol 228.42 Calculated Property
ΔvapH 48.85 kJ/mol 273.85 Calculated Property
ΔvapH 46.33 kJ/mol 319.28 Calculated Property
ΔvapH 43.73 kJ/mol 364.71 Calculated Property
ΔvapH 40.92 kJ/mol 410.14 Calculated Property
ΔvapH 37.78 kJ/mol 455.58 Calculated Property
ΔvapH 34.08 kJ/mol 501.01 Calculated Property
ΔvapH 29.46 kJ/mol 546.44 Calculated Property
ΔvapH 22.85 kJ/mol 591.87 Calculated Property
ΔvapH 0.00 kJ/mol 637.30 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [6.04e-04; 3230.11] kPa [228.42; 637.30] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = exp(A + B/T + C·ln(T) + D·T^E)
Y is Pvap in kPa, T in K
Coefficient A1.11654e+02
Coefficient B-9.56028e+03
Coefficient C-1.43064e+01
Coefficient D9.37525e-06
Coefficient E2.00000e+00
Temperature range, min.228.42
Temperature range, max.637.30
Pvap 6.04e-04 kPa 228.42 Calculated Property
Pvap 0.06 kPa 273.85 Calculated Property
Pvap 1.19 kPa 319.28 Calculated Property
Pvap 9.90 kPa 364.71 Calculated Property
Pvap 46.83 kPa 410.14 Calculated Property
Pvap 153.99 kPa 455.58 Calculated Property
Pvap 398.33 kPa 501.01 Calculated Property
Pvap 878.40 kPa 546.44 Calculated Property
Pvap 1742.89 kPa 591.87 Calculated Property
Pvap 3230.11 kPa 637.30 Calculated Property
Pvap [6.96e-04; 3113.46] kPa [228.46; 637.38] KDB Vapor Pressure Data Show Hide
Equationln(Y) = A + B/T + C·ln(T) + D·T² + E/T²
Y is Pvap in kPa, T in K
Coefficient A8.58665e+01
Coefficient B-8.51220e+03
Coefficient C-1.03429e+01
Coefficient D5.70952e-06
Coefficient E0.00000e+00
Temperature range, min.228.46
Temperature range, max.637.38
Pvap 6.96e-04 kPa 228.46 Calculated Property
Pvap 0.06 kPa 273.90 Calculated Property
Pvap 1.17 kPa 319.33 Calculated Property
Pvap 9.73 kPa 364.77 Calculated Property
Pvap 46.84 kPa 410.20 Calculated Property
Pvap 156.66 kPa 455.64 Calculated Property
Pvap 408.78 kPa 501.07 Calculated Property
Pvap 897.43 kPa 546.51 Calculated Property
Pvap 1744.79 kPa 591.94 Calculated Property
Pvap 3113.46 kPa 637.38 Calculated Property
Pvap [6.41; 103.98] kPa [354.64; 438.87] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42743e+01
Coefficient B-3.61419e+03
Coefficient C-6.35720e+01
ReferenceForziati, Norris, et al., 1949, 2
Temperature range, min.354.64
Temperature range, max.438.87
Pvap 6.41 kPa 354.64 Calculated Property
Pvap 9.43 kPa 364.00 Calculated Property
Pvap 13.57 kPa 373.36 Calculated Property
Pvap 19.10 kPa 382.72 Calculated Property
Pvap 26.37 kPa 392.08 Calculated Property
Pvap 35.77 kPa 401.43 Calculated Property
Pvap 47.73 kPa 410.79 Calculated Property
Pvap 62.72 kPa 420.15 Calculated Property
Pvap 81.28 kPa 429.51 Calculated Property
Pvap 103.98 kPa 438.87 Calculated Property
Pvap [6.41; 103.98] kPa [354.64; 438.87] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.42743e+01
Coefficient B-3.61419e+03
Coefficient C-6.35720e+01
ReferenceForziati, Norris, et al., 1949
Temperature range, min.354.64
Temperature range, max.438.87
Pvap 6.41 kPa 354.64 Calculated Property
Pvap 9.43 kPa 364.00 Calculated Property
Pvap 13.57 kPa 373.36 Calculated Property
Pvap 19.10 kPa 382.72 Calculated Property
Pvap 26.37 kPa 392.08 Calculated Property
Pvap 35.77 kPa 401.43 Calculated Property
Pvap 47.73 kPa 410.79 Calculated Property
Pvap 62.72 kPa 420.15 Calculated Property
Pvap 81.28 kPa 429.51 Calculated Property
Pvap 103.98 kPa 438.87 Calculated Property
Property Value Unit Temperature (K) Source
ρl [914.85; 275.56] kg/m3 [228.42; 637.30] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A / B^(1 + (1 − T/C)^D)
Y is ρl in kg/m3, T in K
Coefficient A7.09359e+01
Coefficient B2.57420e-01
Coefficient C6.37300e+02
Coefficient D2.77240e-01
Temperature range, min.228.42
Temperature range, max.637.30
ρl 914.85 kg/m3 228.42 Calculated Property
ρl 880.25 kg/m3 273.85 Calculated Property
ρl 843.87 kg/m3 319.28 Calculated Property
ρl 805.27 kg/m3 364.71 Calculated Property
ρl 763.81 kg/m3 410.14 Calculated Property
ρl 718.50 kg/m3 455.58 Calculated Property
ρl 667.60 kg/m3 501.01 Calculated Property
ρl 607.66 kg/m3 546.44 Calculated Property
ρl 529.19 kg/m3 591.87 Calculated Property
ρl 275.56 kg/m3 637.30 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.03; 0.01] N/m [228.45; 438.15] Jasper (1972), surface tension of pure liquid compounds Compiled value Show Hide
EquationY = A + B·T + C·T² + D·T³ + E·T⁴
Y is γ in N/m, T in K
Coefficient A5.42916e-02
Coefficient B-8.97000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.228.45
Temperature range, max.438.15
γ 0.03 N/m 228.45 Calculated Property
γ 0.03 N/m 251.75 Calculated Property
γ 0.03 N/m 275.05 Calculated Property
γ 0.03 N/m 298.35 Calculated Property
γ 0.03 N/m 321.65 Calculated Property
γ 0.02 N/m 344.95 Calculated Property
γ 0.02 N/m 368.25 Calculated Property
γ 0.02 N/m 391.55 Calculated Property
γ 0.02 N/m 414.85 Calculated Property
γ 0.01 N/m 438.15 Calculated Property
γ [0.03; 1.73e-05] N/m [228.42; 632.80] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is γ in N/m, T in K
Coefficient A-5.58280e-02
Coefficient B-2.68250e+01
Coefficient C-1.91000e+00
Coefficient D-1.72020e-03
Coefficient E3.88990e-07
CommentRange stopped where the equation turns negative; ChemSep gives it to 637.3 K.
Temperature range, min.228.42
Temperature range, max.632.80
γ 0.03 N/m 228.42 Calculated Property
γ 0.03 N/m 273.35 Calculated Property
γ 0.03 N/m 318.28 Calculated Property
γ 0.02 N/m 363.21 Calculated Property
γ 0.02 N/m 408.15 Calculated Property
γ 0.01 N/m 453.08 Calculated Property
γ 0.01 N/m 498.01 Calculated Property
γ 0.01 N/m 542.94 Calculated Property
γ 0.00 N/m 587.87 Calculated Property
γ 1.73e-05 N/m 632.80 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.08] W/m×K [228.42; 1000.00] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A·T^B / (1 + C/T + D/T²)
Y is λgas in W/m×K, T in K
Coefficient A3.22500e-01
Coefficient B-7.99440e-02
Coefficient C-4.64540e+02
Coefficient D1.93820e+06
Temperature range, min.228.42
Temperature range, max.1000.00
λgas 0.01 W/m×K 228.42 Calculated Property
λgas 0.01 W/m×K 314.15 Calculated Property
λgas 0.02 W/m×K 399.88 Calculated Property
λgas 0.02 W/m×K 485.61 Calculated Property
λgas 0.03 W/m×K 571.34 Calculated Property
λgas 0.04 W/m×K 657.08 Calculated Property
λgas 0.05 W/m×K 742.81 Calculated Property
λgas 0.06 W/m×K 828.54 Calculated Property
λgas 0.07 W/m×K 914.27 Calculated Property
λgas 0.08 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.15; 0.10] W/m×K [223.15; 437.89] ChemSep v8.3 pure component data Compiled value Show Hide
EquationY = A + exp(B/T + C + D·T + E·T²)
Y is λliquid in W/m×K, T in K
Coefficient A-1.25210e-02
Coefficient B7.73980e+01
Coefficient C-2.49120e+00
Coefficient D2.71810e-03
Coefficient E-5.39080e-06
Temperature range, min.223.15
Temperature range, max.437.89
λliquid 0.15 W/m×K 223.15 Calculated Property
λliquid 0.15 W/m×K 247.01 Calculated Property
λliquid 0.14 W/m×K 270.87 Calculated Property
λliquid 0.14 W/m×K 294.73 Calculated Property
λliquid 0.13 W/m×K 318.59 Calculated Property
λliquid 0.13 W/m×K 342.45 Calculated Property
λliquid 0.12 W/m×K 366.31 Calculated Property
λliquid 0.12 W/m×K 390.17 Calculated Property
λliquid 0.11 W/m×K 414.03 Calculated Property
λliquid 0.10 W/m×K 437.89 Calculated Property

Similar Compounds

Benzonitrile, 3,5-dimethyl-. Benzene, 1,3-dimethyl-. 3-Methylbenzyl radical. 5-Methylisophthalonitrile. 3,5-(CH3)2-C6H3-CCH. 3,5-Dimethylbenzaldehyde. «alpha»-Bromomesitylene. 1-Chloromethyl-3,5-dimethylbenzene. m-Xylene, 5-chloro-. Benzene, 1,3-bis-(chloromethyl)-5-methyl. Benzene, 1-iodo-3,5-dimethyl-. 5-Fluoro-m-xylene. Benzene, 1-bromo-3,5-dimethyl-. Benzene, 1,2,3,5-tetramethyl-. benzene, 1,3,5-tris(bromomethyl)-.

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Mixtures

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Sources

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