Chemical Properties of PHENOL, 4-METHYL- (CAS 106-44-5)

PHENOL, 4-METHYL-

InChI
InChI=1S/C7H8O/c1-6-2-4-7(8)5-3-6/h2-5,8H,1H3
InChI Key
IWDCLRJOBJJRNH-UHFFFAOYSA-N
Formula
C7H8O
SMILES
Cc1ccc(O)cc1
Molecular Weight1
108.14
CAS
106-44-5
Other Names
  • 1-Methyl-4-hydroxybenzene
  • 1-hydroxy-4-methylbenzene
  • 4-Cresol
  • 4-Hydroxytoluene
  • 4-methylphenol
  • 4-methylphenol ( p-cresol)
  • Cresol, para
  • Cresol,p-
  • NSC 3696
  • Paracresol
  • Paramethyl phenol
  • Phenol, 4-methyI
  • Rcra waste number U052
  • p-Cresol (4-methylphenol)
  • p-Cresylic acid
  • p-Kresol
  • p-Methylhydroxybenzene
  • p-Methylphenol
  • p-Oxytoluene
  • p-Toluol
  • p-Tolyl alcohol
  • p-cresol
  • p-hydroxytoluene
  • para-cresol
  • para-hydroxytoluene
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Physical Properties

Property Value Unit Source
ω [0.5100; 0.5150]   Show Hide
ω 0.5150 PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
ω 0.5100 ChemSep v8.3 pure component data Compiled value
PAff 814.00 ± 8.00 kJ/mol NIST
BasG 782.00 ± 8.00 kJ/mol NIST
ΔcH°liquid -3705.00 kJ/mol NIST
ΔcH°solid [-3703.00; -3698.60] kJ/mol Show Hide
ΔcH°solid -3698.70 ± 0.30 kJ/mol NIST
ΔcH°solid -3698.60 ± 0.67 kJ/mol NIST
ΔcH°solid -3703.00 kJ/mol NIST
μ 1.56 debye ChemSep v8.3 pure component data Compiled value
ΔfG° -31.66 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas [-125.40; -125.30] kJ/mol Show Hide
ΔfH°gas -125.35 kJ/mol ChemSep v8.3 pure component data Compiled value
ΔfH°gas -125.30 ± 1.50 kJ/mol NIST
ΔfH°gas -125.40 ± 1.50 kJ/mol NIST
ΔfH°liquid -193.00 kJ/mol NIST
ΔfH°solid [-199.30; -199.20] kJ/mol Show Hide
ΔfH°solid -199.20 kJ/mol NIST
ΔfH°solid -199.30 ± 1.50 kJ/mol NIST
ΔfusH° 13.71 kJ/mol Joback Calculated Property
ΔsubH° [73.10; 73.90] kJ/mol Show Hide
ΔsubH° 73.10 ± 0.60 kJ/mol NIST
ΔsubH° 73.90 kJ/mol NIST
ΔsubH° 73.90 ± 1.50 kJ/mol NIST
ΔsubH° 73.90 kJ/mol NIST
ΔvapH° 46.61 kJ/mol NIST
IE [8.13; 8.97] eV Show Hide
IE 8.34 ± 0.03 eV NIST
IE 8.31 ± 0.08 eV NIST
IE 8.13 eV NIST
IE 8.34 eV NIST
IE Outlier 8.97 eV NIST
IE 8.35 eV NIST
IE 8.38 eV NIST
log10WS [-0.73; -0.70]   Show Hide
log10WS -0.70 Aq. Solubility Prediction
log10WS -0.73 Estimated Solubility
logPoct/wat 1.701 Crippen Calculated Property
McVol 91.600 ml/mol McGowan Calculated Property
Pc [4070.00; 5150.00] kPa Show Hide
Pc 4070.00 kPa IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Pc 5147.31 kPa PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Pc 5150.00 kPa ChemSep v8.3 pure component data Compiled value
Pc 4070.00 ± 58.84 kPa NIST
Pc 4559.63 ± 303.98 kPa NIST
Pc 5147.31 ± 81.06 kPa NIST
Ptriple 0.03 kPa ChemSep v8.3 pure component data Compiled value
Inp [175.30; 1104.00]   Show Hide
Inp 1055.00 NIST
Inp 1081.00 NIST
Inp 1055.00 NIST
Inp 1056.00 NIST
Inp 1086.00 NIST
Inp 1047.00 NIST
Inp 1081.00 NIST
Inp 1048.00 NIST
Inp 1045.00 NIST
Inp 1052.00 NIST
Inp 1034.00 NIST
Inp 1033.10 NIST
Inp 1037.00 NIST
Inp 1050.00 NIST
Inp 1049.00 NIST
Inp 1060.00 NIST
Inp 1073.00 NIST
Inp 1063.00 NIST
Inp 1059.00 NIST
Inp 1077.00 NIST
Inp 1098.00 NIST
Inp 1075.00 NIST
Inp 1085.00 NIST
Inp 1082.00 NIST
Inp 1074.00 NIST
Inp 1062.40 NIST
Inp 1064.10 NIST
Inp 1084.00 NIST
Inp 1086.00 NIST
Inp 1074.00 NIST
Inp 1072.00 NIST
Inp 1084.00 NIST
Inp 1051.80 NIST
Inp 1070.00 NIST
Inp 1079.00 NIST
Inp 1085.74 NIST
Inp 1089.67 NIST
Inp 1076.00 NIST
Inp 1078.00 NIST
Inp 1080.00 NIST
Inp 1081.00 NIST
Inp 1082.00 NIST
Inp 1059.00 NIST
Inp 1056.00 NIST
Inp 1054.00 NIST
Inp 1064.00 NIST
Inp 1066.00 NIST
Inp 1048.00 NIST
Inp 1074.00 NIST
Inp 1075.00 NIST
Inp 1078.00 NIST
Inp 1093.00 NIST
Inp 1080.00 NIST
Inp 1077.30 NIST
Inp 1076.00 NIST
Inp 1075.30 NIST
Inp 1093.00 NIST
Inp 1086.00 NIST
Inp 1081.70 NIST
Inp 1077.00 NIST
Inp 1076.00 NIST
Inp 1075.00 NIST
Inp 1086.00 NIST
Inp 1075.00 NIST
Inp 1060.00 NIST
Inp 1055.00 NIST
Inp 1055.00 NIST
Inp 1100.00 NIST
Inp 1074.00 NIST
Inp 1070.00 NIST
Inp 1081.00 NIST
Inp 1075.00 NIST
Inp 1070.00 NIST
Inp 1069.00 NIST
Inp 1051.00 NIST
Inp 1055.00 NIST
Inp 1052.00 NIST
Inp 1041.00 NIST
Inp 1051.00 NIST
Inp 1053.00 NIST
Inp 1056.00 NIST
Inp 1044.00 NIST
Inp 1071.00 NIST
Inp 1052.00 NIST
Inp 1078.00 NIST
Inp 1086.00 NIST
Inp 1052.00 NIST
Inp 1060.00 NIST
Inp 1090.00 NIST
Inp 1074.00 NIST
Inp 1047.00 NIST
Inp 1073.00 NIST
Inp 1070.00 NIST
Inp 1051.00 NIST
Inp 1080.00 NIST
Inp 1081.00 NIST
Inp 1082.00 NIST
Inp 1086.00 NIST
Inp 1044.00 NIST
Inp 1104.00 NIST
Inp 1048.00 NIST
Inp 1046.00 NIST
Inp 1048.00 NIST
Inp 1047.00 NIST
Inp 1071.00 NIST
Inp 1077.00 NIST
Inp 1077.00 NIST
Inp 1093.00 NIST
Inp 1074.00 NIST
Inp 1075.00 NIST
Inp 1079.00 NIST
Inp 1068.00 NIST
Inp 1070.00 NIST
Inp 1073.00 NIST
Inp 1080.00 NIST
Inp 1080.00 NIST
Inp 1046.00 NIST
Inp 1056.00 NIST
Inp 1076.00 NIST
Inp 1060.00 NIST
Inp 1075.00 NIST
Inp 1080.00 NIST
Inp 1072.00 NIST
Inp 1077.00 NIST
Inp 1074.00 NIST
Inp 1075.00 NIST
Inp 1075.00 NIST
Inp 1051.00 NIST
Inp 1073.00 NIST
Inp 1031.00 NIST
Inp 1071.00 NIST
Inp 1087.00 NIST
Inp 1056.00 NIST
Inp 1069.00 NIST
Inp 1074.00 NIST
Inp 1083.00 NIST
Inp 1082.00 NIST
Inp 1081.00 NIST
Inp 1050.00 NIST
Inp 1053.00 NIST
Inp 1057.00 NIST
Inp 1059.00 NIST
Inp 1086.00 NIST
Inp 1052.00 NIST
Inp 1056.00 NIST
Inp 1075.00 NIST
Inp 1051.00 NIST
Inp Outlier 177.37 NIST
Inp Outlier 175.30 NIST
Inp Outlier 175.80 NIST
Inp Outlier 176.95 NIST
Inp Outlier 175.80 NIST
Inp 1059.00 NIST
Inp 1093.00 NIST
Inp 1076.00 NIST
Ip [2031.00; 2126.00]   Show Hide
Ip 2089.00 NIST
Ip 2085.00 NIST
Ip 2093.00 NIST
Ip Outlier 2126.00 NIST
Ip 2050.00 NIST
Ip 2089.00 NIST
Ip 2087.00 NIST
Ip 2053.00 NIST
Ip 2085.00 NIST
Ip 2076.00 NIST
Ip 2090.00 NIST
Ip 2074.00 NIST
Ip Outlier 2037.00 NIST
Ip Outlier 2038.00 NIST
Ip 2078.00 NIST
Ip 2078.00 NIST
Ip 2047.00 NIST
Ip 2103.00 NIST
Ip 2059.00 NIST
Ip 2068.00 NIST
Ip 2077.00 NIST
Ip 2089.00 NIST
Ip 2057.00 NIST
Ip 2069.00 NIST
Ip 2073.00 NIST
Ip 2089.00 NIST
Ip 2091.00 NIST
Ip 2091.00 NIST
Ip 2117.00 NIST
Ip 2081.00 NIST
Ip 2083.00 NIST
Ip 2100.00 NIST
Ip 2094.21 NIST
Ip 2100.99 NIST
Ip 2092.27 NIST
Ip 2091.00 NIST
Ip 2087.00 NIST
Ip 2079.00 NIST
Ip 2052.00 NIST
Ip 2090.00 NIST
Ip 2090.00 NIST
Ip 2082.00 NIST
Ip 2083.00 NIST
Ip 2048.00 NIST
Ip 2049.00 NIST
Ip 2100.00 NIST
Ip 2067.00 NIST
Ip 2105.00 NIST
Ip Outlier 2123.00 NIST
Ip 2071.00 NIST
Ip 2077.00 NIST
Ip 2079.00 NIST
Ip 2073.00 NIST
Ip 2105.00 NIST
Ip 2080.00 NIST
Ip 2093.00 NIST
Ip 2090.00 NIST
Ip 2076.00 NIST
Ip Outlier 2121.00 NIST
Ip 2071.00 NIST
Ip 2096.00 NIST
Ip 2083.00 NIST
Ip 2085.00 NIST
Ip 2100.00 NIST
Ip 2068.00 NIST
Ip 2082.00 NIST
Ip 2050.00 NIST
Ip 2080.00 NIST
Ip 2044.00 NIST
Ip 2084.00 NIST
Ip 2050.00 NIST
Ip 2070.00 NIST
Ip 2098.00 NIST
Ip Outlier 2031.00 NIST
Ip 2079.00 NIST
Ip 2060.00 NIST
Ip Outlier 2031.00 NIST
Ip 2090.00 NIST
Ip 2100.00 NIST
Ip 2110.00 NIST
Ip 2080.00 NIST
Ip 2083.00 NIST
Ip 2092.00 NIST
Ip 2100.00 NIST
Ip 2056.00 NIST
Ip 2063.00 NIST
Ip 2060.00 NIST
Ip 2060.00 NIST
Ip 2066.00 NIST
Ip 2094.00 NIST
Ip 2094.00 NIST
Ip 2072.00 NIST
Ip 2078.00 NIST
Ip 2074.00 NIST
Ip 2094.00 NIST
Ip 2077.00 NIST
Ip 2087.00 NIST
Ip 2094.00 NIST
Ip 2048.00 NIST
Ip 2054.00 NIST
Ip 2055.00 NIST
Ip 2071.00 NIST
Ip 2080.00 NIST
Ip 2068.00 NIST
Ip 2084.00 NIST
Ip 2079.00 NIST
Ip 2093.00 NIST
Ip Outlier 2123.00 NIST
Ip 2089.00 NIST
S°solid,1 bar 167.32 J/mol×K NIST
Tboil [473.70; 475.65] K Show Hide
Tboil 474.85 K Experimental and predicted vapor-liquid equilibrium for binary systems with diethanolamine, m-cresol and p-cresol at 20.0 kPa
Tboil 475.12 K ChemSep v8.3 pure component data Compiled value
Tboil 475.10 K NIST
Tboil 475.05 ± 0.40 K NIST
Tboil 474.65 ± 1.00 K NIST
Tboil 475.03 ± 0.30 K NIST
Tboil 474.85 ± 1.00 K NIST
Tboil 475.25 ± 1.00 K NIST
Tboil 474.85 ± 0.40 K NIST
Tboil 475.47 ± 1.00 K NIST
Tboil 475.65 ± 0.20 K NIST
Tboil 475.65 ± 1.00 K NIST
Tboil Outlier 473.70 ± 1.00 K NIST
Tboil 475.15 ± 1.00 K NIST
Tboil 474.95 ± 2.00 K NIST
Tc [699.00; 704.60] K Show Hide
Tc 704.60 K IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value
Tc 704.60 K PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Tc 704.50 K ChemSep v8.3 pure component data Compiled value
Tc 704.60 ± 0.40 K NIST
Tc 704.55 ± 0.30 K NIST
Tc 699.00 ± 3.00 K NIST
Tc 699.20 ± 5.00 K NIST
Tfus [305.15; 309.00] K Show Hide
Tfus 307.90 K The fusion thermochemistry of self-associated aromatic compounds at 298.15 K studied by solution calorimetry
Tfus 307.15 K Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value
Tfus 307.93 K ChemSep v8.3 pure component data Compiled value
Tfus 306.05 K Aq. Solubility Prediction
Tfus 307.00 ± 0.10 K NIST
Tfus 307.84 ± 0.05 K NIST
Tfus 307.15 ± 1.00 K NIST
Tfus 307.88 ± 0.05 K NIST
Tfus 307.93 ± 0.10 K NIST
Tfus 307.85 ± 0.50 K NIST
Tfus 307.75 ± 0.30 K NIST
Tfus 307.55 ± 0.50 K NIST
Tfus 306.15 ± 1.50 K NIST
Tfus 307.55 ± 0.60 K NIST
Tfus 307.70 ± 0.20 K NIST
Tfus 307.30 ± 0.30 K NIST
Tfus Outlier 305.15 ± 0.50 K NIST
Tfus 306.95 ± 0.20 K NIST
Tfus 307.15 ± 0.50 K NIST
Tfus Outlier 309.00 ± 1.00 K NIST
Ttriple [307.93; 307.94] K Show Hide
Ttriple 307.93 K ChemSep v8.3 pure component data Compiled value
Ttriple 307.94 ± 0.02 K NIST
Ttriple 307.94 ± 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 [0.277; 0.332] m3/kmol Show Hide
Vc 0.332 m3/kmol PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value
Vc 0.277 m3/kmol ChemSep v8.3 pure component data Compiled value
Zc 0.2440000 ChemSep v8.3 pure component data Compiled value

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,solid [150.25; 226.20] J/mol×K [298.15; 313.00] Show Hide
Cp,solid 163.50 J/mol×K 298.15 NIST
Cp,solid 221.03 J/mol×K 298.15 NIST
Cp,solid 150.25 J/mol×K 298.15 NIST
Cp,solid 226.20 J/mol×K 313.00 NIST
η [0.0018910; 0.0084440] Pa×s [308.15; 353.15] Show Hide
η 0.0084440 Pa×s 308.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0067450 Pa×s 313.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0054710 Pa×s 318.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0045320 Pa×s 323.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0038880 Pa×s 328.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0032450 Pa×s 333.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0024310 Pa×s 343.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
η 0.0018910 Pa×s 353.15 Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
ΔfusH [8.58; 12.72] kJ/mol [307.35; 309.00] Show Hide
ΔfusH 11.80 kJ/mol 307.35 NIST
ΔfusH 11.80 kJ/mol 307.40 NIST
ΔfusH 8.58 kJ/mol 307.60 NIST
ΔfusH 12.72 kJ/mol 307.90 NIST
ΔfusH 12.72 kJ/mol 307.90 NIST
ΔfusH 12.71 kJ/mol 307.94 NIST
ΔfusH 12.71 kJ/mol 307.94 NIST
ΔfusH 12.60 kJ/mol 308.80 NIST
ΔfusH 11.89 kJ/mol 309.00 NIST
ΔfusH 12.25 kJ/mol 309.00 NIST
ΔsubH 73.90 ± 1.50 kJ/mol 290.00 NIST
ΔvapH [46.00; 62.00] kJ/mol [350.50; 579.00] Show Hide
ΔvapH 62.00 kJ/mol 350.50 NIST
ΔvapH 55.60 kJ/mol 428.00 NIST
ΔvapH 55.40 kJ/mol 431.00 NIST
ΔvapH 51.30 kJ/mol 446.50 NIST
ΔvapH 49.20 kJ/mol 498.00 NIST
ΔvapH 46.00 kJ/mol 579.00 NIST
n0 [1.53100; 1.53910]   [298.15; 308.15] Show Hide
n0 1.53900 298.15 Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
n0 1.53910 298.15 Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
n0 1.53910 298.15 Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
n0 1.53910 298.15 Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
n0 1.53700 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 1.53400 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 1.53100 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 [994.59; 1154.00] kg/m3 [293.15; 343.15] Show Hide
ρl 1034.09 kg/m3 293.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1154.00 kg/m3 298.15 Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
ρl 1030.25 kg/m3 298.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1026.47 kg/m3 303.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1025.90 kg/m3 303.15 Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
ρl 1026.39 kg/m3 303.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1022.50 kg/m3 308.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1022.56 kg/m3 308.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1018.59 kg/m3 313.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1018.64 kg/m3 313.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1018.80 kg/m3 313.15 Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
ρl 1018.80 kg/m3 313.15 Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
ρl 1014.68 kg/m3 318.15 Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
ρl 1014.66 kg/m3 318.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1010.70 kg/m3 323.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1011.30 kg/m3 323.20 Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
ρl 1006.72 kg/m3 328.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 1002.70 kg/m3 333.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 998.66 kg/m3 338.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ρl 994.59 kg/m3 343.15 Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
ΔfusS [38.00; 41.26] J/mol×K [307.35; 309.00] Show Hide
ΔfusS 38.00 J/mol×K 307.35 NIST
ΔfusS 41.26 J/mol×K 307.94 NIST
ΔfusS 41.26 J/mol×K 307.94 NIST
ΔfusS 38.47 J/mol×K 309.00 NIST
ΔfusS 39.60 J/mol×K 309.00 NIST

Datasets

Mass density, kg/m3

Fixed Measured
Temperature, K - Liquid Pressure, kPa - Liquid Mass density, kg/m3 - Liquid
312.90 1002.00 1019.4
312.90 2016.00 1020.0
312.90 3017.00 1020.6
312.90 4016.00 1021.1
312.90 5002.00 1021.7
312.90 6010.00 1022.2
312.90 7000.00 1022.8
312.90 8006.00 1023.3
312.90 9001.00 1023.9
312.90 10002.00 1024.4
312.90 11006.00 1024.9
312.90 12002.00 1025.5
312.90 13015.00 1026.0
312.90 14007.00 1026.6
312.90 15006.00 1027.1
312.90 16019.00 1027.6
312.90 17004.00 1028.1
312.90 18011.00 1028.6
312.90 19009.00 1029.2
312.90 20005.00 1029.7
312.90 21008.00 1030.2
312.90 22004.00 1030.7
312.90 23023.00 1031.2
312.90 24004.00 1031.7
312.90 25006.00 1032.2
322.78 1019.00 1011.6
322.78 2015.00 1012.2
322.78 3002.00 1012.8
322.78 4013.00 1013.4
322.78 5011.00 1013.9
322.78 6018.00 1014.5
322.78 7022.00 1015.1
322.78 8001.00 1015.7
322.78 9015.00 1016.3
322.78 10006.00 1016.8
322.78 11002.00 1017.4
322.78 12018.00 1017.9
322.78 13002.00 1018.4
322.78 14016.00 1019.0
322.78 15001.00 1019.5
322.78 16000.00 1020.1
322.78 17001.00 1020.6
322.78 18029.00 1021.2
322.78 19015.00 1021.7
322.78 20011.00 1022.2
322.78 21022.00 1022.8
322.78 22002.00 1023.3
322.78 23006.00 1023.8
322.78 24010.00 1024.4
322.78 25023.00 1024.9
332.54 1040.00 1003.7
332.54 2019.00 1004.3
332.54 3013.00 1005.0
332.54 4019.00 1005.6
332.54 5001.00 1006.2
332.54 6001.00 1006.8
332.54 7002.00 1007.5
332.54 8041.00 1008.1
332.54 9000.00 1008.7
332.54 10001.00 1009.2
332.54 11006.00 1009.7
332.54 12001.00 1010.4
332.54 13008.00 1010.9
332.54 14004.00 1011.5
332.54 15003.00 1012.1
332.54 16015.00 1012.7
332.54 17011.00 1013.3
332.54 18014.00 1013.9
332.54 19014.00 1014.4
332.54 20009.00 1014.9
332.54 21013.00 1015.4
332.54 22007.00 1016.0
332.54 23000.00 1016.6
332.54 24001.00 1017.1
332.54 25032.00 1017.7
342.37 1001.00 995.7
342.37 2002.00 996.4
342.37 3004.00 997.1
342.37 4025.00 997.7
342.37 5036.00 998.2
342.37 6032.00 998.8
342.37 7001.00 999.3
342.37 8020.00 999.9
342.37 9003.00 1000.6
342.37 10002.00 1001.3
342.37 11036.00 1001.9
342.37 12001.00 1002.6
342.37 13020.00 1003.2
342.37 14019.00 1003.9
342.37 15007.00 1004.5
342.37 16000.00 1005.1
342.37 17022.00 1005.6
342.37 18014.00 1006.2
342.37 19033.00 1006.8
342.37 20005.00 1007.4
342.37 21005.00 1007.9
342.37 22010.00 1008.4
342.37 22962.00 1009.0
342.37 24021.00 1009.7
342.37 25017.00 1010.2
352.15 1023.00 987.9
352.15 2007.00 988.5
352.15 3000.00 989.1
352.15 4003.00 989.8
352.15 5001.00 990.4
352.15 6009.00 991.1
352.15 7001.00 991.7
352.15 8037.00 992.4
352.15 9008.00 993.0
352.15 10040.00 993.7
352.15 11006.00 994.3
352.15 12001.00 994.9
352.15 13001.00 995.5
352.15 14009.00 996.2
352.15 15000.00 996.8
352.15 16010.00 997.4
352.15 17028.00 998.0
352.15 18020.00 998.6
352.15 19045.00 999.3
352.15 20018.00 1000.0
352.15 21038.00 1000.5
352.15 22000.00 1001.1
352.15 23065.00 1001.8
352.15 24024.00 1002.4
352.15 25039.00 1002.9
361.90 1017.00 979.6
361.90 1991.00 980.3
361.90 3004.00 981.0
361.90 4027.00 981.5
361.90 4992.00 982.3
361.90 6000.00 983.1
361.90 7033.00 983.6
361.90 8010.00 984.4
361.90 9001.00 985.0
361.90 9998.00 985.8
361.90 10994.00 986.5
361.90 11976.00 987.0
361.90 12949.00 987.7
361.90 14010.00 988.3
361.90 15017.00 989.0
361.90 15992.00 989.6
361.90 16992.00 990.3
361.90 18007.00 990.8
361.90 19034.00 991.6
361.90 19992.00 992.1
361.90 21000.00 992.9
361.90 22059.00 993.4
361.90 23020.00 994.1
361.90 24014.00 994.8
361.90 25002.00 995.3
Reference

Correlations

Property Value Unit Temperature (K) Source
Cp,gas [86.60; 321.26] J/mol×K [200.00; 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 A5.87480e+01
Coefficient B-5.29020e+02
Coefficient C5.97924e+00
Coefficient D-3.51000e-05
Coefficient E-1.61310e-09
Temperature range, min.200.00
Temperature range, max.1500.00
Cp,gas 86.60 J/mol×K 200.00 Calculated Property
Cp,gas 142.77 J/mol×K 344.44 Calculated Property
Cp,gas 190.33 J/mol×K 488.89 Calculated Property
Cp,gas 226.26 J/mol×K 633.33 Calculated Property
Cp,gas 253.32 J/mol×K 777.78 Calculated Property
Cp,gas 274.01 J/mol×K 922.22 Calculated Property
Cp,gas 290.12 J/mol×K 1066.67 Calculated Property
Cp,gas 302.84 J/mol×K 1211.11 Calculated Property
Cp,gas 313.03 J/mol×K 1355.56 Calculated Property
Cp,gas 321.26 J/mol×K 1500.00 Calculated Property
Property Value Unit Temperature (K) Source
Cp,liquid [227.49; 257.82] J/mol×K [307.93; 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 A1.42400e+02
Coefficient B6.25270e+02
Coefficient C-3.61336e+00
Coefficient D2.81800e-02
Coefficient E-2.79580e-05
Temperature range, min.307.93
Temperature range, max.400.00
Cp,liquid 227.49 J/mol×K 307.93 Calculated Property
Cp,liquid 231.31 J/mol×K 318.16 Calculated Property
Cp,liquid 235.13 J/mol×K 328.39 Calculated Property
Cp,liquid 238.92 J/mol×K 338.62 Calculated Property
Cp,liquid 242.61 J/mol×K 348.85 Calculated Property
Cp,liquid 246.15 J/mol×K 359.08 Calculated Property
Cp,liquid 249.49 J/mol×K 369.31 Calculated Property
Cp,liquid 252.58 J/mol×K 379.54 Calculated Property
Cp,liquid 255.38 J/mol×K 389.77 Calculated Property
Cp,liquid 257.82 J/mol×K 400.00 Calculated Property
Property Value Unit Temperature (K) Source
η [0.0922874; 0.0000336] Pa×s [273.15; 563.72] 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-8.20785e+02
Coefficient B3.55229e+04
Coefficient C1.24397e+02
Coefficient D-1.27538e-04
Coefficient E2.00000e+00
Temperature range, min.273.15
Temperature range, max.563.72
η 0.0922874 Pa×s 273.15 Calculated Property
η 0.0099069 Pa×s 305.44 Calculated Property
η 0.0027906 Pa×s 337.72 Calculated Property
η 0.0013385 Pa×s 370.01 Calculated Property
η 0.0008298 Pa×s 402.29 Calculated Property
η 0.0005546 Pa×s 434.58 Calculated Property
η 0.0003536 Pa×s 466.86 Calculated Property
η 0.0001978 Pa×s 499.15 Calculated Property
η 0.0000915 Pa×s 531.43 Calculated Property
η 0.0000336 Pa×s 563.72 Calculated Property
Property Value Unit Temperature (K) Source
ΔvapH [66.85; 0.00] kJ/mol [307.93; 704.50] 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 A1.36170e+02
Coefficient B1.40400e+00
Coefficient C8.09100e-01
Coefficient D-3.60550e+00
Coefficient E2.02680e+00
Critical temperature, Tc (K)7.04500e+02
CommentRange stopped at Tc; ChemSep gives it to 704.65 K.
Temperature range, min.307.93
Temperature range, max.704.50
ΔvapH 66.85 kJ/mol 307.93 Calculated Property
ΔvapH 60.95 kJ/mol 351.99 Calculated Property
ΔvapH 55.83 kJ/mol 396.06 Calculated Property
ΔvapH 51.28 kJ/mol 440.12 Calculated Property
ΔvapH 47.01 kJ/mol 484.18 Calculated Property
ΔvapH 42.64 kJ/mol 528.25 Calculated Property
ΔvapH 37.64 kJ/mol 572.31 Calculated Property
ΔvapH 31.17 kJ/mol 616.37 Calculated Property
ΔvapH 21.63 kJ/mol 660.44 Calculated Property
ΔvapH 0.00 kJ/mol 704.50 Calculated Property
Property Value Unit Temperature (K) Source
Pvap [0.03; 5147.39] kPa [307.93; 704.65] 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 A2.30013e+02
Coefficient B-1.72153e+04
Coefficient C-3.12864e+01
Coefficient D1.63766e-05
Coefficient E2.00000e+00
Temperature range, min.307.93
Temperature range, max.704.65
Pvap 0.03 kPa 307.93 Calculated Property
Pvap 0.73 kPa 352.01 Calculated Property
Pvap 7.20 kPa 396.09 Calculated Property
Pvap 37.70 kPa 440.17 Calculated Property
Pvap 130.47 kPa 484.25 Calculated Property
Pvap 344.63 kPa 528.33 Calculated Property
Pvap 764.49 kPa 572.41 Calculated Property
Pvap 1520.57 kPa 616.49 Calculated Property
Pvap 2839.77 kPa 660.57 Calculated Property
Pvap 5147.39 kPa 704.65 Calculated Property
Pvap [0.03; 5097.40] kPa [307.93; 704.65] 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 A1.76963e+02
Coefficient B-1.46480e+04
Coefficient C-2.33776e+01
Coefficient D1.14084e-05
Coefficient E0.00000e+00
Temperature range, min.307.93
Temperature range, max.704.65
Pvap 0.03 kPa 307.93 Calculated Property
Pvap 0.73 kPa 352.01 Calculated Property
Pvap 6.92 kPa 396.09 Calculated Property
Pvap 36.30 kPa 440.17 Calculated Property
Pvap 128.36 kPa 484.25 Calculated Property
Pvap 347.63 kPa 528.33 Calculated Property
Pvap 785.54 kPa 572.41 Calculated Property
Pvap 1571.32 kPa 616.49 Calculated Property
Pvap 2901.34 kPa 660.57 Calculated Property
Pvap 5097.40 kPa 704.65 Calculated Property
Pvap [8.88; 101.42] kPa [401.20; 475.03] NIST Show Hide
Equationln(Y) = A + B/(T + C)
Y is Pvap in kPa, T in K
Coefficient A1.41400e+01
Coefficient B-3.45061e+03
Coefficient C-1.12600e+02
ReferenceDreisbach and Shrader, 1949
CommentCoefficents calculated by NIST from author's data.
Temperature range, min.401.20
Temperature range, max.475.03
Pvap 8.88 kPa 401.20 Calculated Property
Pvap 12.36 kPa 409.40 Calculated Property
Pvap 16.89 kPa 417.61 Calculated Property
Pvap 22.72 kPa 425.81 Calculated Property
Pvap 30.09 kPa 434.01 Calculated Property
Pvap 39.31 kPa 442.22 Calculated Property
Pvap 50.69 kPa 450.42 Calculated Property
Pvap 64.58 kPa 458.62 Calculated Property
Pvap 81.35 kPa 466.83 Calculated Property
Pvap 101.42 kPa 475.03 Calculated Property
Property Value Unit Temperature (K) Source
ρl [1024.91; 374.82] kg/m3 [307.89; 704.65] 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 A1.02534e+02
Coefficient B2.87700e-01
Coefficient C7.04660e+02
Coefficient D2.87300e-01
Temperature range, min.307.89
Temperature range, max.704.65
ρl 1024.91 kg/m3 307.89 Calculated Property
ρl 989.51 kg/m3 351.97 Calculated Property
ρl 952.20 kg/m3 396.06 Calculated Property
ρl 912.52 kg/m3 440.14 Calculated Property
ρl 869.77 kg/m3 484.23 Calculated Property
ρl 822.89 kg/m3 528.31 Calculated Property
ρl 770.05 kg/m3 572.40 Calculated Property
ρl 707.50 kg/m3 616.48 Calculated Property
ρl 625.12 kg/m3 660.57 Calculated Property
ρl 374.82 kg/m3 704.65 Calculated Property
Property Value Unit Temperature (K) Source
γ [0.04; 0.02] N/m [307.95; 475.15] 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 A6.48570e-02
Coefficient B-9.62000e-05
Coefficient C0.00000e+00
Coefficient D0.00000e+00
Coefficient E0.00000e+00
Temperature range, min.307.95
Temperature range, max.475.15
γ 0.04 N/m 307.95 Calculated Property
γ 0.03 N/m 326.53 Calculated Property
γ 0.03 N/m 345.11 Calculated Property
γ 0.03 N/m 363.68 Calculated Property
γ 0.03 N/m 382.26 Calculated Property
γ 0.03 N/m 400.84 Calculated Property
γ 0.02 N/m 419.42 Calculated Property
γ 0.02 N/m 437.99 Calculated Property
γ 0.02 N/m 456.57 Calculated Property
γ 0.02 N/m 475.15 Calculated Property
γ [0.04; 0.00] N/m [293.15; 683.77] 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-5.16620e-02
Coefficient B1.04810e+01
Coefficient C-2.22690e+00
Coefficient D-6.01820e-04
Coefficient E-6.50930e-07
Temperature range, min.293.15
Temperature range, max.683.77
γ 0.04 N/m 293.15 Calculated Property
γ 0.03 N/m 336.55 Calculated Property
γ 0.03 N/m 379.95 Calculated Property
γ 0.02 N/m 423.36 Calculated Property
γ 0.02 N/m 466.76 Calculated Property
γ 0.02 N/m 510.16 Calculated Property
γ 0.01 N/m 553.56 Calculated Property
γ 0.01 N/m 596.97 Calculated Property
γ 0.01 N/m 640.37 Calculated Property
γ 0.00 N/m 683.77 Calculated Property
Property Value Unit Temperature (K) Source
λgas [0.01; 0.07] W/m×K [307.93; 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 A1.67350e-04
Coefficient B9.38390e-01
Coefficient C5.92490e+02
Coefficient D2.57040e+04
Temperature range, min.307.93
Temperature range, max.1000.00
λgas 0.01 W/m×K 307.93 Calculated Property
λgas 0.02 W/m×K 384.83 Calculated Property
λgas 0.02 W/m×K 461.72 Calculated Property
λgas 0.03 W/m×K 538.62 Calculated Property
λgas 0.03 W/m×K 615.52 Calculated Property
λgas 0.04 W/m×K 692.41 Calculated Property
λgas 0.05 W/m×K 769.31 Calculated Property
λgas 0.05 W/m×K 846.21 Calculated Property
λgas 0.06 W/m×K 923.10 Calculated Property
λgas 0.07 W/m×K 1000.00 Calculated Property
Property Value Unit Temperature (K) Source
λliquid [0.14; 0.12] W/m×K [293.15; 475.13] 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 A6.17710e-02
Coefficient B-1.23880e+02
Coefficient C-1.18230e+00
Coefficient D-3.33390e-03
Coefficient E1.01510e-06
Temperature range, min.293.15
Temperature range, max.475.13
λliquid 0.14 W/m×K 293.15 Calculated Property
λliquid 0.14 W/m×K 313.37 Calculated Property
λliquid 0.14 W/m×K 333.59 Calculated Property
λliquid 0.14 W/m×K 353.81 Calculated Property
λliquid 0.13 W/m×K 374.03 Calculated Property
λliquid 0.13 W/m×K 394.25 Calculated Property
λliquid 0.13 W/m×K 414.47 Calculated Property
λliquid 0.13 W/m×K 434.69 Calculated Property
λliquid 0.12 W/m×K 454.91 Calculated Property
λliquid 0.12 W/m×K 475.13 Calculated Property

Similar Compounds

4-OH-benzyl. 4-Me-phenoxy. Phenol, 3-methyl-. 1,2-Benzenediol, 4-methyl-. 3-OH-benzyl. Benzenemethanol, 4-hydroxy-. Benzene, 1,1'-oxybis[4-methyl-. 1,3-benzenediol, 4-methyl-. Benzaldehyde, 4-hydroxy-. Benzene, 1-methoxy-4-methyl-. 3-Me-phenoxy. Phenol, 2,4-dimethyl-. PHENOL, 3,4-DIMETHYL-. Phenol, 2-methyl-. Phosphorous acid, tris(4-methylphenyl) ester.

Find more compounds similar to PHENOL, 4-METHYL-.

Mixtures

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Sources

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