- 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
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- ΔcH°solid : Standard solid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°solid : Solid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| 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 |
|
| 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 |
|
| 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 |
|
| 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 |
|
| 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 |
|
| 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] |
|
|
| log10WS | -0.70 | Aq. Sol... | |
| log10WS | -0.73 | Estimat... | |
| logPoct/wat | 1.701 | Crippen Calculated Property | |
| McVol | 91.600 | ml/mol | McGowan Calculated Property |
| Pc | [4070.00; 5147.31] | kPa |
|
| 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] |
|
|
| 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] |
|
|
| 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 |
|
| Tboil | 474.85 | K | Experim... |
| 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 |
|
| 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 |
|
| Tfus | 306.05 | K | Aq. Sol... |
| 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 | 0.285 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [184.27; 237.56] | J/mol×K | [466.86; 696.68] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 180 190 200 210 220 230 240 500 600 700 | ||||
| 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] |
|
| 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] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 8.00e-3 9.00e-3 320 340 | ||||
| η | 0.0084440 | Pa×s | 308.15 | Excess ... |
| η | 0.0067450 | Pa×s | 313.15 | Excess ... |
| η | 0.0054710 | Pa×s | 318.15 | Excess ... |
| η | 0.0045320 | Pa×s | 323.15 | Excess ... |
| η | 0.0038880 | Pa×s | 328.15 | Excess ... |
| η | 0.0032450 | Pa×s | 333.15 | Excess ... |
| η | 0.0024310 | Pa×s | 343.15 | Excess ... |
| η | 0.0018910 | Pa×s | 353.15 | Excess ... |
| ΔfusH | [8.58; 12.72] | kJ/mol | [307.35; 309.00] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 9 10 11 12 13 307.5 308 308.5 309 | ||||
| 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] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 45 50 55 60 400 500 | ||||
| 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] |
|
|
|
T(K) Refractive Index 1.53 1.53 1.54 1.54 300 305 | ||||
| n0 | 1.53900 | 298.15 | Activit... | |
| n0 | 1.53910 | 298.15 | Excess ... | |
| n0 | 1.53910 | 298.15 | Excess ... | |
| n0 | 1.53910 | 298.15 | Activit... | |
| n0 | 1.53700 | 298.15 | Densiti... | |
| n0 | 1.53400 | 303.15 | Densiti... | |
| n0 | 1.53100 | 308.15 | Densiti... | |
| ρl | [994.59; 1154.00] | kg/m3 | [293.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 1000 1050 1100 1150 300 320 340 | ||||
| ρl | 1034.09 | kg/m3 | 293.15 | Experim... |
| ρl | 1030.25 | kg/m3 | 298.15 | Experim... |
| ρl | 1154.00 | kg/m3 | 298.15 | Bubble ... |
| ρl | 1025.90 | kg/m3 | 303.15 | Vapor-L... |
| ρl | 1026.39 | kg/m3 | 303.15 | Experim... |
| ρl | 1026.47 | kg/m3 | 303.15 | Thermod... |
| ρl | 1022.50 | kg/m3 | 308.15 | Experim... |
| ρl | 1022.56 | kg/m3 | 308.15 | Thermod... |
| ρl | 1018.80 | kg/m3 | 313.15 | Liquid-... |
| ρl | 1018.80 | kg/m3 | 313.15 | Liquid-... |
| ρl | 1018.64 | kg/m3 | 313.15 | Thermod... |
| ρl | 1018.59 | kg/m3 | 313.15 | Experim... |
| ρl | 1014.68 | kg/m3 | 318.15 | Thermod... |
| ρl | 1014.66 | kg/m3 | 318.15 | Experim... |
| ρl | 1010.70 | kg/m3 | 323.15 | Experim... |
| ρl | 1011.30 | kg/m3 | 323.20 | Liquid-... |
| ρl | 1006.72 | kg/m3 | 328.15 | Experim... |
| ρl | 1002.70 | kg/m3 | 333.15 | Experim... |
| ρl | 998.66 | kg/m3 | 338.15 | Experim... |
| ρl | 994.59 | kg/m3 | 343.15 | Experim... |
| ΔfusS | [38.00; 41.26] | J/mol×K | [307.35; 309.00] |
|
| 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 Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.76963e+02 | |||
| Coefficient B | -1.46480e+04 | |||
| Coefficient C | -2.33776e+01 | |||
| Coefficient D | 1.14084e-05 | |||
| Temperature range, min. | 307.93 | |||
| Temperature range, max. | 704.65 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 | ||||
| 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
Find more compounds similar to p-Cresol.
Mixtures
- p-Cresol + Methyl Alcohol
- 1-Propanol + p-Cresol
- p-Cresol + 1-Butanol
- p-Cresol + Ethanol
- p-Cresol + Isopropyl Alcohol
- p-Cresol + 1-Propanol, 2-methyl-
- 2-Propanol, 2-methyl- + p-Cresol
- Benzene, nitro- + p-Cresol
- p-Cresol + Formamide, N,N-dimethyl-
- p-Cresol + Ethane, 1,2-dichloro-
- p-Cresol + Ethane, 1,1,2,2-tetrachloro-
- Trichloroethylene + p-Cresol
- p-Cresol + Tetrachloroethylene
- p-Cresol + o-Xylene
- p-Cresol + Benzene, 1,3-dimethyl-
- p-Cresol + p-Xylene
- p-Cresol + Ethylbenzene
- p-Cresol + Water
- p-Cresol + Eucalyptol + Water
- p-Cresol + 2-Hexanone + Water
Find more mixtures with p-Cresol.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Activity coefficients of the binary mixtures of a-cresol or p-cresol with C l-C4 aliphatic alcohols near ambient pressure
- Excess Gibbs energies of binary mixtures formed by nitrobenzene with selected compounds at 94.95 kPa
- Excess Gibbs' energies of the binary mixtures formed by N,N-dimethylformamide with xylenes and cresols at 95.1 kPa
- Liquid-liquid equilibria in the ternary systems water + cresols + methyl butyl ketone at 298.2 and 313.2 K: experimental data and correlation
- Liquid-liquid equilibria for the extraction of phenols from alkane using ethylene glycol
- Liquid-liquid equilibria for methyl isobutyl ketone + cresols + water at 333.15K, 343.15K and 353.15K: Experimental results and data correlation
- Determination and modeling of liquid-liquid equilibrium for ternary mixtures of methyl isopropyl ketone, cresol isomers and water
- Measurement, correlation and COSMO-SAC prediction of liquid-liquid equilibrium for the ternary systems, mesityl oxide + o-, m-, p-cresol + water, at 333.2 K and 353.2 K
- Phase equilibria of phenolic compounds in water or ethanol
- Activity coefficients and excess Gibbs free energy of some binary mixtures formed by p-cresol at 95.23 kPa
- Bubble point measurements of binary mixtures formed by ethyl benzene with selected compounds at 95.35 kPa
- Volumetric and ultrasonic behaviour of binary mixtures of 1-nonanol with o-cresol, m-cresol, p-cresol and anisole at T = (293.15 and 313.15) K
- Excess parameters of binary mixtures of anisaldehyde with o-cresol, m-cresol and p-cresol at T = (303.15, 308.15, 313.15, and 318.15) K
- Measurement and thermodynamic modeling of ternary (liquid + liquid) equilibrium for extraction of o-cresol, m-cresol or p-cresol from aqueous solution with 2-pentanone
- (Liquid + liquid) extraction of phenols from aqueous solutions with cineole
- Liquid-liquid equilibria for toluene/heptane + phenol/cresols + ethylene glycol system
- Extraction of o-, m- and p-cresol from aqueous solution with methyl isopropyl ketone: Equilibrium, correlations, and COSMO-RS predictions
- Liquid-liquid equilibrium for methyl butyl ketone + o-, m-, p-cresol + water ternary systems and COSMO-SAC predictions
- Experimental and predicted vapor-liquid equilibrium for binary systems with diethanolamine, m-cresol and p-cresol at 20.0 kPa
- Thermodynamic and spectroscopic study of molecular interactions between ethanol and isomeric cresols
- Liquid Liquid Equilibrium for the Ternary Systems Methyl tert-Butyl Ketone + o-, m-, p-Cresol + Water at (298.2, 313.2, and 323.2) K
- Phase Equilibrium on Extraction Methylphenols from Aqueous Solution with 3,3-Dimethyl-2-butanone at 333.2 K and 353.2 K
- Excess Molar Volumes and Viscosities of Binary Mixtures of p-Cresol with Ethylene Glycol and Methanol at Different Temperature and Atmospheric Pressure
- Liquid-Liquid Equilibria in Ternary Systems of Aromatic Hydrocarbons (Toluene or Ethylbenzene) + Phenols + Water
- 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
- Henry's Law Constants and Infinite Dilution Activity Coefficients of Propane, Propene, Butane, 2-Methylpropane, 1-Butene, 2-Methylpropene, trans-2-Butene, cis-2-Butene, 1,3-Butadiene, Dimethyl Ether, Chloroethane, and 1,1-Difluoroethane in 2-Methylphenol, 3-Methylphenol, and 4-Methylphenol
- Liquid-Liquid(-Liquid) Equilibria in Ternary Systems of Aliphatic Hydrocarbons (Heptane or Octane) + Phenols + Water
- Vapor-Liquid Equilibria in Ternary Systems of Toluene or Octane + Phenols + Water
- Densities of Cresols and Linear Alkane Mixtures at High Pressure
- Experimental Densities and Speeds of Sound of Substituted Phenols and Their Modeling with the Prigogine Flory Patterson Model
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
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