Chemical Properties of p-Cresol (CAS 106-44-5)

p-Cresol

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-Hydroxy-4-methylbenzene
  • 1-Methyl-4-hydroxybenzene
  • 4-Cresol
  • 4-Hydroxytoluene
  • 4-Methylphenol
  • 4-methylphenol ( p-cresol)
  • Cresol, para
  • Cresol,p-
  • NSC 3696
  • Paracresol
  • Paramethyl phenol
  • Phenol, 4-methyI
  • Phenol, 4-methyl-
  • Rcra waste number U052
  • p-Cresol (4-methylphenol)
  • p-Cresylic acid
  • p-Hydroxytoluene
  • p-Kresol
  • p-Methylhydroxybenzene
  • p-Methylphenol
  • p-Oxytoluene
  • p-Toluol
  • p-Tolyl alcohol
  • para-cresol
  • para-hydroxytoluene
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Physical Properties

Property Value Unit Source
ω 0.4877 Relay (1.0) Calculated Property
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
ΔfG° -34.15 kJ/mol Joback Calculated Property
ΔfH°gas [-125.40; -125.30] kJ/mol Show Hide
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; 5147.31] kPa Show Hide
Pc 4070.00 ± 58.84 kPa NIST
Pc 4559.63 ± 303.98 kPa NIST
Pc 5147.31 ± 81.06 kPa NIST
Inp [175.30; 1104.00]   Show Hide
Inp 1045.00 NIST
Inp 1052.00 NIST
Inp 1052.00 NIST
Inp 1052.00 NIST
Inp 1034.00 NIST
Inp 1033.10 NIST
Inp 1037.00 NIST
Inp 1037.00 NIST
Inp 1050.00 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 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 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 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 1060.00 NIST
Inp 1075.00 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
Inp 1055.00 NIST
Inp 1081.00 NIST
Inp 1056.00 NIST
Inp 1086.00 NIST
Inp 1047.00 NIST
Inp 1048.00 NIST
I [2031.00; 2126.00]   Show Hide
I 2089.00 NIST
I 2085.00 NIST
I 2093.00 NIST
I Outlier 2126.00 NIST
I 2050.00 NIST
I 2089.00 NIST
I 2087.00 NIST
I 2053.00 NIST
I 2085.00 NIST
I 2076.00 NIST
I 2090.00 NIST
I 2074.00 NIST
I Outlier 2037.00 NIST
I Outlier 2038.00 NIST
I 2078.00 NIST
I 2078.00 NIST
I 2047.00 NIST
I 2103.00 NIST
I 2059.00 NIST
I 2068.00 NIST
I 2077.00 NIST
I 2089.00 NIST
I 2057.00 NIST
I 2069.00 NIST
I 2073.00 NIST
I 2089.00 NIST
I 2091.00 NIST
I 2091.00 NIST
I 2117.00 NIST
I 2081.00 NIST
I 2083.00 NIST
I 2100.00 NIST
I 2094.21 NIST
I 2100.99 NIST
I 2092.27 NIST
I 2091.00 NIST
I 2087.00 NIST
I 2079.00 NIST
I 2052.00 NIST
I 2090.00 NIST
I 2090.00 NIST
I 2082.00 NIST
I 2083.00 NIST
I 2048.00 NIST
I 2049.00 NIST
I 2100.00 NIST
I 2067.00 NIST
I 2105.00 NIST
I Outlier 2123.00 NIST
I 2071.00 NIST
I 2077.00 NIST
I 2079.00 NIST
I 2073.00 NIST
I 2105.00 NIST
I 2080.00 NIST
I 2093.00 NIST
I 2090.00 NIST
I 2076.00 NIST
I Outlier 2121.00 NIST
I 2071.00 NIST
I 2096.00 NIST
I 2083.00 NIST
I 2085.00 NIST
I 2100.00 NIST
I 2068.00 NIST
I 2082.00 NIST
I 2050.00 NIST
I 2080.00 NIST
I 2044.00 NIST
I 2084.00 NIST
I 2050.00 NIST
I 2070.00 NIST
I 2098.00 NIST
I Outlier 2031.00 NIST
I 2079.00 NIST
I 2060.00 NIST
I Outlier 2031.00 NIST
I 2090.00 NIST
I 2100.00 NIST
I 2110.00 NIST
I 2080.00 NIST
I 2083.00 NIST
I 2092.00 NIST
I 2100.00 NIST
I 2056.00 NIST
I 2063.00 NIST
I 2060.00 NIST
I 2060.00 NIST
I 2066.00 NIST
I 2094.00 NIST
I 2094.00 NIST
I 2072.00 NIST
I 2078.00 NIST
I 2074.00 NIST
I 2094.00 NIST
I 2077.00 NIST
I 2087.00 NIST
I 2094.00 NIST
I 2048.00 NIST
I 2054.00 NIST
I 2055.00 NIST
I Outlier 2123.00 NIST
I 2093.00 NIST
I 2071.00 NIST
I 2080.00 NIST
I 2068.00 NIST
I 2084.00 NIST
I 2079.00 NIST
I 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 475.10 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 ± 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 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 309.00 ± 1.00 K NIST
Ttriple 307.94 ± 0.02 K NIST
Vc 0.305 m3/kmol Relay (1.0) Calculated Property

Temperature Dependent Properties

Property Value Unit Temperature (K) Source
Cp,gas [184.27; 237.56] J/mol×K [466.86; 696.68] Show Hide
Cp,gas 184.27 J/mol×K 466.86 Joback Calculated Property
Cp,gas 195.06 J/mol×K 505.16 Joback Calculated Property
Cp,gas 204.98 J/mol×K 543.47 Joback Calculated Property
Cp,gas 214.11 J/mol×K 581.77 Joback Calculated Property
Cp,gas 222.53 J/mol×K 620.08 Joback Calculated Property
Cp,gas 230.32 J/mol×K 658.38 Joback Calculated Property
Cp,gas 237.56 J/mol×K 696.68 Joback Calculated Property
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 12.60 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 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
Pvap [0.03; 5097.40] kPa [307.93; 704.65] KDB Vapor Pressure Data Show Hide
Equationln(Pvp) = A + B/T + C*ln(T) + D*T^2
Coefficient A1.76963e+02
Coefficient B-1.46480e+04
Coefficient C-2.33776e+01
Coefficient D1.14084e-05
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

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 p-Cresol.

Mixtures

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Sources

Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more. Take the time to validate and double check the source of the data.
Outlier This icon means that the value is more than 2 standard deviations away from the property mean.