Chemical Properties of Phenol, 2-methyl- (CAS 95-48-7)

Phenol, 2-methyl-

InChI
InChI=1S/C7H8O/c1-6-4-2-3-5-7(6)8/h2-5,8H,1H3
InChI Key
QWVGKYWNOKOFNN-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1ccccc1O
Molecular Weight1
108.14
CAS
95-48-7
Other Names
  • 1-Methyl-2-hydroxybenzene
  • 1-hydroxy-2-methylbenzene
  • 2-Hydroxytoluene
  • 2-cresol
  • 2-methylphenol
  • NSC 23076
  • Orthocresol
  • Rcra waste number U052
  • o-Cresylic acid
  • o-Kresol
  • o-Methylphenylol
  • o-Oxytoluene
  • o-Toluol
  • o-cresol
  • o-hydroxytoluene
  • o-methylphenol
  • ortho-cresol
  • ortho-hydroxytoluene
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Physical Properties

Property Value Unit Source
ω [0.4330; 0.4430]   Show Hide
ω 0.4430 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.4350 ChemSep v8.3 pure component data Compiled value
ω 0.4330 KDB
PAff 832.00 ± 8.00 kJ/mol NIST
BasG 800.00 ± 8.00 kJ/mol NIST
ΔcH°liquid -3696.00 kJ/mol NIST
ΔcH°solid [-3697.00; -3693.30] kJ/mol Show Hide
ΔcH°solid -3693.60 ± 0.42 kJ/mol NIST
ΔcH°solid -3693.30 ± 1.00 kJ/mol NIST
ΔcH°solid -3697.00 kJ/mol NIST
μ [1.45; 1.60] debye Show Hide
μ 1.45 debye ChemSep v8.3 pure component data Compiled value
μ 1.60 debye KDB
ΔfG° [-35.43; -33.00] kJ/mol Show Hide
ΔfG° -35.43 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfG° -33.00 kJ/mol KDB
ΔfH°gas [-128.70; -128.30] kJ/mol Show Hide
ΔfH°gas -128.57 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -128.70 kJ/mol KDB
ΔfH°gas -128.30 ± 0.88 kJ/mol NIST
ΔfH°gas -128.60 ± 0.92 kJ/mol NIST
ΔfH°liquid -202.00 kJ/mol NIST
ΔfH°solid [-204.60; -204.30] kJ/mol Show Hide
ΔfH°solid -204.30 kJ/mol NIST
ΔfH°solid -204.60 ± 0.92 kJ/mol NIST
ΔfusH° 13.71 kJ/mol Joback Calculated Property
ΔsubH° [73.70; 76.02] kJ/mol Show Hide
ΔsubH° 73.70 ± 0.50 kJ/mol NIST
ΔsubH° 76.00 kJ/mol NIST
ΔsubH° 76.02 ± 0.75 kJ/mol NIST
ΔsubH° 76.00 kJ/mol NIST
ΔvapH° 44.89 kJ/mol NIST
IE [8.14; 8.93] eV Show Hide
IE 8.14 eV NIST
IE 8.24 ± 0.02 eV NIST
IE 8.93 eV NIST
IE 8.46 ± 0.06 eV NIST
IE 8.50 eV NIST
IE 8.48 eV NIST
log10WS [-0.62; -0.62]   Show Hide
log10WS -0.62 Aq. Solubility Prediction
log10WS -0.62 Estimated Solubility
logPoct/wat 1.701 Crippen Calculated Property
McVol 91.600 ml/mol McGowan Calculated Property
NFPA Fire 2 KDB
NFPA Health 2 KDB
Pc [4170.00; 5010.00] kPa Show Hide
Pc 4170.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 5005.45 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 5000.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 5010.00 kPa KDB
Pc 4170.00 ± 39.22 kPa NIST
Pc 4863.60 ± 303.98 kPa NIST
Pc 5005.46 ± 70.92 kPa NIST
Ptriple 0.07 kPa ChemSep v8.3 pure component data Compiled value
Inp [170.20; 1080.00]   Show Hide
Inp 1030.00 NIST
Inp 1027.00 NIST
Inp 1032.00 NIST
Inp 1014.30 NIST
Inp 1017.60 NIST
Inp 1007.00 NIST
Inp 1008.00 NIST
Inp 1029.00 NIST
Inp 1030.00 NIST
Inp 1030.00 NIST
Inp 1040.00 NIST
Inp 1048.00 NIST
Inp 1078.00 NIST
Inp 1039.00 NIST
Inp 1035.00 NIST
Inp 1052.00 NIST
Inp 1042.70 NIST
Inp 1071.00 NIST
Inp 1073.00 NIST
Inp 1031.10 NIST
Inp 1054.00 NIST
Inp 1080.00 NIST
Inp 1042.00 NIST
Inp 1029.70 NIST
Inp 1032.00 NIST
Inp 1042.00 NIST
Inp 1044.00 NIST
Inp 1029.00 NIST
Inp 1055.00 NIST
Inp 1068.00 NIST
Inp 1068.00 NIST
Inp 1051.80 NIST
Inp 1052.90 NIST
Inp 1052.00 NIST
Inp 1030.00 NIST
Inp 1034.00 NIST
Inp 1034.00 NIST
Inp 1054.00 NIST
Inp 1077.00 NIST
Inp 1072.00 NIST
Inp 1053.00 NIST
Inp 1054.00 NIST
Inp 1058.00 NIST
Inp 1060.00 NIST
Inp 1054.00 NIST
Inp 1030.00 NIST
Inp 1033.00 NIST
Inp 1052.00 NIST
Inp 1053.00 NIST
Inp 1027.00 NIST
Inp 1038.00 NIST
Inp 1015.00 NIST
Inp 1076.00 NIST
Inp 1076.00 NIST
Inp 1024.00 NIST
Inp 1024.00 NIST
Inp 1058.00 NIST
Inp 1051.00 NIST
Inp 1057.00 NIST
Inp 1068.00 NIST
Inp 1077.00 NIST
Inp 1053.00 NIST
Inp 1044.00 NIST
Inp 1044.00 NIST
Inp 1059.00 NIST
Inp 1030.00 NIST
Inp 1044.00 NIST
Inp 1050.00 NIST
Inp 1037.00 NIST
Inp 1040.00 NIST
Inp 1053.00 NIST
Inp 1066.00 NIST
Inp 1079.00 NIST
Inp 1065.00 NIST
Inp 1063.00 NIST
Inp 1030.00 NIST
Inp 1036.00 NIST
Inp 1035.00 NIST
Inp 1050.00 NIST
Inp 1055.00 NIST
Inp 1035.00 NIST
Inp Outlier 170.20 NIST
Inp Outlier 170.30 NIST
Inp Outlier 172.54 NIST
Inp Outlier 170.90 NIST
Inp Outlier 171.30 NIST
Inp Outlier 172.86 NIST
Inp Outlier 172.86 NIST
Inp Outlier 173.57 NIST
Inp 1035.00 NIST
Inp Outlier 172.86 NIST
Inp Outlier 170.20 NIST
Ip [1959.00; 2053.00]   Show Hide
Ip 2004.00 NIST
Ip 1980.00 NIST
Ip 2014.00 NIST
Ip 1995.00 NIST
Ip 2022.00 NIST
Ip 2019.00 NIST
Ip Outlier 1959.00 NIST
Ip 2011.00 NIST
Ip 2011.00 NIST
Ip 2000.00 NIST
Ip 2000.00 NIST
Ip Outlier 1969.00 NIST
Ip 2000.00 NIST
Ip 2000.00 NIST
Ip 2019.80 NIST
Ip 2017.19 NIST
Ip 2020.19 NIST
Ip 2014.43 NIST
Ip 2033.00 NIST
Ip 2011.00 NIST
Ip 2012.00 NIST
Ip 2002.00 NIST
Ip 2000.00 NIST
Ip 2021.00 NIST
Ip 1992.00 NIST
Ip 1993.00 NIST
Ip 1992.00 NIST
Ip 2011.00 NIST
Ip 2030.00 NIST
Ip 2008.00 NIST
Ip 1995.00 NIST
Ip Outlier 2050.00 NIST
Ip 2007.00 NIST
Ip 2025.00 NIST
Ip 2025.00 NIST
Ip 2010.00 NIST
Ip 2010.00 NIST
Ip 1980.00 NIST
Ip 2030.00 NIST
Ip Outlier 2053.00 NIST
Ip 2012.00 NIST
Ip 1996.00 NIST
Ip 2000.00 NIST
Ip 1970.00 NIST
Ip 1979.00 NIST
Ip 1979.00 NIST
Ip 2014.00 NIST
Ip 2010.00 NIST
Ip 2012.00 NIST
Ip 1979.00 NIST
Ip 2004.00 NIST
Ip 2000.00 NIST
Ip 2011.00 NIST
Ip 2007.00 NIST
S°solid,1 bar 165.44 J/mol×K NIST
Tboil [460.90; 464.95] K Show Hide
Tboil 464.17 K ChemSep v8.3 pure component data Compiled value
Tboil 464.19 K KDB
Tboil 464.20 K NIST
Tboil 463.75 ± 2.00 K NIST
Tboil 464.10 ± 0.30 K NIST
Tboil 464.25 ± 1.00 K NIST
Tboil 464.30 ± 0.60 K NIST
Tboil 463.95 ± 1.00 K NIST
Tboil 464.25 ± 0.30 K NIST
Tboil 464.25 ± 0.35 K NIST
Tboil Outlier 460.90 ± 0.70 K NIST
Tboil 464.95 ± 1.50 K NIST
Tboil 464.65 ± 1.50 K NIST
Tboil 464.15 ± 0.50 K NIST
Tc [695.15; 697.60] K Show Hide
Tc 697.60 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 697.60 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 697.60 K ChemSep v8.3 pure component data Compiled value
Tc 697.60 K KDB
Tc 697.60 ± 0.40 K NIST
Tc 697.55 ± 0.23 K NIST
Tc 695.15 ± 2.00 K NIST
Tc 695.50 ± 3.00 K NIST
Tfus [302.55; 304.65] K Show Hide
Tfus 304.15 K Liquid pharmaceuticals formulation by eutectic formation
Tfus 304.65 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 304.19 K ChemSep v8.3 pure component data Compiled value
Tfus 302.90 K KDB
Tfus 304.60 K Aq. Solubility Prediction
Tfus 304.00 ± 0.30 K NIST
Tfus 304.14 ± 0.05 K NIST
Tfus 304.05 ± 0.30 K NIST
Tfus 304.09 ± 0.05 K NIST
Tfus 304.09 ± 0.10 K NIST
Tfus 303.55 ± 0.25 K NIST
Tfus 303.50 ± 0.20 K NIST
Tfus 303.55 ± 0.50 K NIST
Tfus 303.70 ± 0.50 K NIST
Tfus 302.65 ± 0.40 K NIST
Tfus 303.45 ± 0.40 K NIST
Tfus 303.75 ± 0.20 K NIST
Tfus 303.60 ± 0.30 K NIST
Tfus 302.55 ± 0.50 K NIST
Tfus 302.90 ± 0.15 K NIST
Ttriple [304.19; 304.20] K Show Hide
Ttriple 304.19 K ChemSep v8.3 pure component data Compiled value
Ttriple 304.20 ± 0.02 K NIST
Ttriple 304.20 ± 0.02 K NIST
UQi 3.89 ChemSep v8.3 pure component data Compiled value
URi 4.76 ChemSep v8.3 pure component data Compiled value
Vc [0.282; 0.282] m3/kmol Show Hide
Vc 0.282 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.282 m3/kmol ChemSep v8.3 pure component data Compiled value
Vc 0.282 m3/kmol KDB
Zc [0.2430000; 0.2435810]   Show Hide
Zc 0.2430000 ChemSep v8.3 pure component data Compiled value
Zc 0.2435810 KDB

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,liquid [225.90; 233.60] J/mol×K [283.00; 313.00] Show Hide
Cp,liquid 225.90 J/mol×K 283.00 NIST
Cp,liquid 233.60 J/mol×K 313.00 NIST
Cp,solid 154.56 J/mol×K 298.15 NIST
η [0.0055660; 0.0132800] Pa×s [288.15; 308.15] Show Hide
η 0.0132800 Pa×s 288.15 Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η 0.0096800 Pa×s 293.15 Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η 0.0077600 Pa×s 298.15 Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η 0.0065750 Pa×s 303.15 Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
η 0.0055660 Pa×s 308.15 Viscosity, Gibbs Free Energy, and Refractive Indices for Binary Mixtures of o-Cresol + Poly(ethylene glycols) at T = 288.15-308.15 K and 96.5 kPa
ΔfusH [13.94; 15.90] kJ/mol [303.00; 305.40] Show Hide
ΔfusH 13.94 kJ/mol 303.00 NIST
ΔfusH 14.80 kJ/mol 304.05 NIST
ΔfusH 15.90 kJ/mol 304.10 NIST
ΔfusH 14.80 kJ/mol 304.10 NIST
ΔfusH 15.82 kJ/mol 304.20 NIST
ΔfusH 15.82 kJ/mol 304.20 NIST
ΔfusH 15.82 kJ/mol 304.20 NIST
ΔfusH 15.82 kJ/mol 304.20 NIST
ΔfusH 14.80 kJ/mol 305.40 NIST
ΔsubH [74.80; 76.00] kJ/mol [288.00; 288.00] Show Hide
ΔsubH 74.80 kJ/mol 288.00 NIST
ΔsubH 76.00 ± 0.80 kJ/mol 288.00 NIST
ΔvapH [44.00; 58.50] kJ/mol [356.50; 573.50] Show Hide
ΔvapH 58.50 kJ/mol 356.50 NIST
ΔvapH 51.30 kJ/mol 428.00 NIST
ΔvapH 50.10 kJ/mol 434.50 NIST
ΔvapH 48.20 kJ/mol 438.50 NIST
ΔvapH 45.19 kJ/mol 464.10 KDB
ΔvapH 46.20 kJ/mol 494.50 NIST
ΔvapH 44.00 kJ/mol 573.50 NIST
n0 [1.53699; 1.54680]   [293.15; 308.15] Show Hide
n0 1.54670 293.15 Bubble points of some binary mixtures formed by o-cresol at 95.75 kPa
n0 1.54680 293.15 Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n0 1.54680 298.15 Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0 1.54670 298.15 Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
n0 1.54400 298.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0 1.54099 303.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
n0 1.53860 308.15 Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
n0 1.53699 308.15 Densities, Speeds of Sound, and Refractive Indices of Binary Mixtures of Decan-1-ol with Anisole, o-Cresol, m-Cresol, and p-Cresol at T = (298.15, 303.15, and 308.15) K
ρl [1001.46; 1046.00] kg/m3 [293.15; 343.15] Show Hide
ρl 1045.77 kg/m3 293.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1046.00 kg/m3 293.15 Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl 1041.41 kg/m3 298.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1036.94 kg/m3 303.15 Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl 1037.05 kg/m3 303.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1037.02 kg/m3 303.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1032.58 kg/m3 308.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1032.73 kg/m3 308.15 Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
ρl 1032.73 kg/m3 308.15 Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
ρl 1032.64 kg/m3 308.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1028.00 kg/m3 313.00 KDB
ρl 1028.19 kg/m3 313.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1028.25 kg/m3 313.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1023.82 kg/m3 318.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1023.83 kg/m3 318.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1019.39 kg/m3 323.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1018.80 kg/m3 323.20 Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
ρl 1014.93 kg/m3 328.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1010.46 kg/m3 333.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1005.97 kg/m3 338.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1001.46 kg/m3 343.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ΔfusS [46.00; 52.00] J/mol×K [303.00; 304.20] Show Hide
ΔfusS 46.00 J/mol×K 303.00 NIST
ΔfusS 49.00 J/mol×K 304.05 NIST
ΔfusS 52.00 J/mol×K 304.20 NIST
ΔfusS 52.00 J/mol×K 304.20 NIST
γ 0.03 N/m 333.20 KDB

Pressure Dependent Properties

Property Value Unit Pressure (kPa) Source
Tboil(P) 411.26 K 20.00 Measurement and correlation of isobaric vapour-liquid equilibrium for systems of o-cresol, m-cresol and 2, 6-dimethylphenol at 20.0 kPa

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
313.20 1022.00 1027.5
313.20 2031.00 1028.1
313.20 3017.00 1028.7
313.20 4012.00 1029.2
313.20 5018.00 1029.8
313.20 6010.00 1030.4
313.20 7005.00 1030.9
313.20 8006.00 1031.5
313.20 9004.00 1032.0
313.20 10005.00 1032.6
323.16 1013.00 1018.7
323.16 2039.00 1019.3
323.16 3007.00 1019.9
323.16 4009.00 1020.5
323.16 5005.00 1021.1
323.16 6004.00 1021.7
323.16 6999.00 1022.2
323.16 8008.00 1022.8
323.16 9002.00 1023.4
323.16 10005.00 1024.0
333.10 1010.00 1009.9
333.10 2033.00 1010.5
333.10 3009.00 1011.1
333.10 4014.00 1011.8
333.10 5004.00 1012.4
333.10 5998.00 1013.0
333.10 7000.00 1013.6
333.10 8009.00 1014.2
333.10 9004.00 1014.8
333.10 10010.00 1015.4
343.06 1023.00 1000.8
343.06 2024.00 1001.6
343.06 3015.00 1002.2
343.06 4003.00 1002.9
343.06 5009.00 1003.6
343.06 6005.00 1004.2
343.06 7008.00 1004.8
343.06 8003.00 1005.5
343.06 8999.00 1006.1
343.06 10004.00 1006.7
352.99 1043.00 991.9
352.99 2000.00 992.6
352.99 3034.00 993.3
352.99 4015.00 994.0
352.99 5033.00 994.6
352.99 6007.00 995.3
352.99 7016.00 996.0
352.99 8006.00 996.7
352.99 9015.00 997.3
352.99 10014.00 998.0
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [75.23; 321.80] 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 A6.43670e+01
Coefficient B-5.35920e+02
Coefficient C5.96324e+00
Coefficient D-3.33830e-05
Coefficient E-2.27590e-09
Temperature range, min.150.00
Temperature range, max.1500.00
Cp,gas 75.23 J/mol×K 150.00 Calculated Property
Cp,gas 128.86 J/mol×K 300.00 Calculated Property
Cp,gas 180.74 J/mol×K 450.00 Calculated Property
Cp,gas 220.26 J/mol×K 600.00 Calculated Property
Cp,gas 249.74 J/mol×K 750.00 Calculated Property
Cp,gas 272.02 J/mol×K 900.00 Calculated Property
Cp,gas 289.18 J/mol×K 1050.00 Calculated Property
Cp,gas 302.61 J/mol×K 1200.00 Calculated Property
Cp,gas 313.27 J/mol×K 1350.00 Calculated Property
Cp,gas 321.80 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [233.26; 252.17] J/mol×K [304.19; 400.00] 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 A1.46600e+02
Coefficient B-1.16230e+02
Coefficient C4.10124e+00
Coefficient D3.45960e-03
Coefficient E-3.34460e-06
Temperature range, min.304.19
Temperature range, max.400.00
Cp,liquid 233.26 J/mol×K 304.19 Calculated Property
Cp,liquid 235.70 J/mol×K 314.84 Calculated Property
Cp,liquid 238.06 J/mol×K 325.48 Calculated Property
Cp,liquid 240.33 J/mol×K 336.13 Calculated Property
Cp,liquid 242.53 J/mol×K 346.77 Calculated Property
Cp,liquid 244.63 J/mol×K 357.42 Calculated Property
Cp,liquid 246.65 J/mol×K 368.06 Calculated Property
Cp,liquid 248.59 J/mol×K 378.71 Calculated Property
Cp,liquid 250.42 J/mol×K 389.35 Calculated Property
Cp,liquid 252.17 J/mol×K 400.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0095328; 0.0000886] Pa×s [293.15; 558.04] 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-4.55077e+02
Coefficient B2.06708e+04
Coefficient C6.78777e+01
Coefficient D-6.60983e-05
Coefficient E2.00000e+00
Temperature range, min.293.15
Temperature range, max.558.04
η 0.0095328 Pa×s 293.15 Calculated Property
η 0.0030570 Pa×s 322.58 Calculated Property
η 0.0014536 Pa×s 352.01 Calculated Property
η 0.0008752 Pa×s 381.45 Calculated Property
η 0.0005997 Pa×s 410.88 Calculated Property
η 0.0004343 Pa×s 440.31 Calculated Property
η 0.0003154 Pa×s 469.74 Calculated Property
η 0.0002213 Pa×s 499.18 Calculated Property
η 0.0001459 Pa×s 528.61 Calculated Property
η 0.0000886 Pa×s 558.04 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [60.08; 0.00] kJ/mol [304.19; 697.60] 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 A9.97210e+01
Coefficient B1.03330e+00
Coefficient C8.04300e-02
Coefficient D-1.21930e+00
Coefficient E5.81240e-01
Critical temperature, Tc (K)6.97600e+02
CommentRange stopped at Tc; ChemSep gives it to 697.65 K.
Temperature range, min.304.19
Temperature range, max.697.60
ΔvapH 60.08 kJ/mol 304.19 Calculated Property
ΔvapH 55.74 kJ/mol 347.90 Calculated Property
ΔvapH 51.70 kJ/mol 391.61 Calculated Property
ΔvapH 47.88 kJ/mol 435.33 Calculated Property
ΔvapH 44.16 kJ/mol 479.04 Calculated Property
ΔvapH 40.37 kJ/mol 522.75 Calculated Property
ΔvapH 36.23 kJ/mol 566.46 Calculated Property
ΔvapH 31.18 kJ/mol 610.18 Calculated Property
ΔvapH 23.87 kJ/mol 653.89 Calculated Property
ΔvapH 0.00 kJ/mol 697.60 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [1.33; 202.65] kPa [352.96; 491.67] The Yaws Handbook of Vapor Pressure Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.46886e+01
Coefficient B-3.72850e+03
Coefficient C-9.40520e+01
Temperature range, min.352.96
Temperature range, max.491.67
Pvap 1.33 kPa 352.96 Calculated Property
Pvap 2.99 kPa 368.37 Calculated Property
Pvap 6.17 kPa 383.78 Calculated Property
Pvap 11.82 kPa 399.20 Calculated Property
Pvap 21.27 kPa 414.61 Calculated Property
Pvap 36.26 kPa 430.02 Calculated Property
Pvap 59.00 kPa 445.43 Calculated Property
Pvap 92.16 kPa 460.85 Calculated Property
Pvap 138.85 kPa 476.26 Calculated Property
Pvap 202.65 kPa 491.67 Calculated Property
Pvap [0.07; 5006.72] kPa [303.15; 697.60] 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 A1.33602e+02
Coefficient B-1.18190e+04
Coefficient C-1.71630e+01
Coefficient D8.70430e-06
Coefficient E2.00000e+00
CommentRange stopped at Tc; ChemSep gives it to 697.65 K.
Temperature range, min.303.15
Temperature range, max.697.60
Pvap 0.07 kPa 303.15 Calculated Property
Pvap 1.22 kPa 346.98 Calculated Property
Pvap 9.55 kPa 390.81 Calculated Property
Pvap 44.56 kPa 434.63 Calculated Property
Pvap 146.52 kPa 478.46 Calculated Property
Pvap 379.01 kPa 522.29 Calculated Property
Pvap 830.24 kPa 566.12 Calculated Property
Pvap 1620.87 kPa 609.94 Calculated Property
Pvap 2924.46 kPa 653.77 Calculated Property
Pvap 5006.72 kPa 697.60 Calculated Property
Pvap [0.06; 5016.43] kPa [304.19; 697.55] 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 A1.36184e+02
Coefficient B-1.20881e+04
Coefficient C-1.74841e+01
Coefficient D8.51800e-06
Coefficient E0.00000e+00
Temperature range, min.304.19
Temperature range, max.697.55
Pvap 0.06 kPa 304.19 Calculated Property
Pvap 1.17 kPa 347.90 Calculated Property
Pvap 9.37 kPa 391.60 Calculated Property
Pvap 44.45 kPa 435.31 Calculated Property
Pvap 147.77 kPa 479.02 Calculated Property
Pvap 384.51 kPa 522.72 Calculated Property
Pvap 843.73 kPa 566.43 Calculated Property
Pvap 1644.20 kPa 610.14 Calculated Property
Pvap 2952.18 kPa 653.84 Calculated Property
Pvap 5016.43 kPa 697.55 Calculated Property
Pvap [10.13; 101.22] kPa [393.37; 464.10] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.37413e+01
Coefficient B-3.20366e+03
Coefficient C-1.12974e+02
ReferenceDreisbach and Shrader, 1949
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.393.37
Temperature range, max.464.10
Pvap 10.13 kPa 393.37 Calculated Property
Pvap 13.84 kPa 401.23 Calculated Property
Pvap 18.58 kPa 409.09 Calculated Property
Pvap 24.58 kPa 416.95 Calculated Property
Pvap 32.06 kPa 424.81 Calculated Property
Pvap 41.27 kPa 432.66 Calculated Property
Pvap 52.49 kPa 440.52 Calculated Property
Pvap 66.00 kPa 448.38 Calculated Property
Pvap 82.14 kPa 456.24 Calculated Property
Pvap 101.22 kPa 464.10 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1060.37; 574.81] kg/m3 [273.15; 676.85] 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 A1.20195e+02
Coefficient B3.09520e-01
Coefficient C6.97600e+02
Coefficient D3.11610e-01
Temperature range, min.273.15
Temperature range, max.676.85
ρl 1060.37 kg/m3 273.15 Calculated Property
ρl 1024.55 kg/m3 318.01 Calculated Property
ρl 987.06 kg/m3 362.86 Calculated Property
ρl 947.50 kg/m3 407.72 Calculated Property
ρl 905.34 kg/m3 452.57 Calculated Property
ρl 859.73 kg/m3 497.43 Calculated Property
ρl 809.33 kg/m3 542.28 Calculated Property
ρl 751.61 kg/m3 587.14 Calculated Property
ρl 680.79 kg/m3 631.99 Calculated Property
ρl 574.81 kg/m3 676.85 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [303.15; 464.15] 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 A6.70455e-02
Coefficient B-1.01100e-04
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.303.15
Temperature range, max.464.15
γ 0.04 N/m 303.15 Calculated Property
γ 0.03 N/m 321.04 Calculated Property
γ 0.03 N/m 338.93 Calculated Property
γ 0.03 N/m 356.82 Calculated Property
γ 0.03 N/m 374.71 Calculated Property
γ 0.03 N/m 392.59 Calculated Property
γ 0.03 N/m 410.48 Calculated Property
γ 0.02 N/m 428.37 Calculated Property
γ 0.02 N/m 446.26 Calculated Property
γ 0.02 N/m 464.15 Calculated Property
γ [0.04; 4.54e-05] N/m [283.15; 697.55] 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-9.43710e-03
Coefficient B2.91180e+02
Coefficient C-4.99440e+00
Coefficient D5.71860e-03
Coefficient E-8.36530e-06
Temperature range, min.283.15
Temperature range, max.697.55
γ 0.04 N/m 283.15 Calculated Property
γ 0.03 N/m 329.19 Calculated Property
γ 0.03 N/m 375.24 Calculated Property
γ 0.02 N/m 421.28 Calculated Property
γ 0.02 N/m 467.33 Calculated Property
γ 0.02 N/m 513.37 Calculated Property
γ 0.01 N/m 559.42 Calculated Property
γ 0.01 N/m 605.46 Calculated Property
γ 0.00 N/m 651.51 Calculated Property
γ 4.54e-05 N/m 697.55 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.07] W/m×K [304.19; 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 A1.86480e-04
Coefficient B9.30200e-01
Coefficient C7.09370e+02
Coefficient D-3.65960e-03
Temperature range, min.304.19
Temperature range, max.1000.00
λgas 0.01 W/m×K 304.19 Calculated Property
λgas 0.02 W/m×K 381.50 Calculated Property
λgas 0.02 W/m×K 458.81 Calculated Property
λgas 0.03 W/m×K 536.13 Calculated Property
λgas 0.03 W/m×K 613.44 Calculated Property
λgas 0.04 W/m×K 690.75 Calculated Property
λgas 0.05 W/m×K 768.06 Calculated Property
λgas 0.05 W/m×K 845.38 Calculated Property
λgas 0.06 W/m×K 922.69 Calculated Property
λgas 0.07 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.15; 0.13] W/m×K [293.15; 464.15] 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 A6.54710e-02
Coefficient B9.23510e+01
Coefficient C-2.84150e+00
Coefficient D1.22450e-03
Coefficient E-2.99560e-06
Temperature range, min.293.15
Temperature range, max.464.15
λliquid 0.15 W/m×K 293.15 Calculated Property
λliquid 0.15 W/m×K 312.15 Calculated Property
λliquid 0.15 W/m×K 331.15 Calculated Property
λliquid 0.15 W/m×K 350.15 Calculated Property
λliquid 0.14 W/m×K 369.15 Calculated Property
λliquid 0.14 W/m×K 388.15 Calculated Property
λliquid 0.14 W/m×K 407.15 Calculated Property
λliquid 0.14 W/m×K 426.15 Calculated Property
λliquid 0.13 W/m×K 445.15 Calculated Property
λliquid 0.13 W/m×K 464.15 Calculated Property

Similar Compounds

2-OH-benzyl. 2-Me-phenoxy. 1,3-benzenediol, 4-methyl-. 2,6-DIHYDROXYTOLUENE. Phenol, 2,4-dimethyl-. Phenol, 2,6-dimethyl-. 1,4-Benzenediol, 2-methyl-. Phenol, 2,5-dimethyl-. 1,2-Benzenediol, 3-methyl-. Phenol, 2,3-dimethyl-. Phenol, 3-methyl-. 4-CHLORO-O-CRESOL. Phenol, 2-methyl-4-iodo. 3-OH-benzyl. Salicyl-3,4,5,6-d4-aldehyde-d.

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Mixtures

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