- InChI
- InChI=1S/C8H10O/c1-6-3-4-8(9)7(2)5-6/h3-5,9H,1-2H3
- InChI Key
- KUFFULVDNCHOFZ-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- Cc1ccc(O)c(C)c1
- Molecular Weight1
- 122.16
- CAS
- 105-67-9
- Other Names
-
- 1,3-Dimethyl-4-hydroxybenzene
- 1-hydroxy-2,4-dimethylbenzene
- 2,4-dimethylphenol
- 2,4-xylenol
- 4,6-Dimethylphenol
- 4-Hydroxy-1,3-dimethylbenzene
- NSC 3829
- Rcra waste number U101
- m-Xylenol
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- 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).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- λgas : Gas thermal conductivity (W/m×K).
- λliquid : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.5136; 0.5136] |
|
|
| ω | 0.5136 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5136 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -4348.47 ± 0.92 | kJ/mol | NIST |
| μ | [1.39; 2.00] | debye |
|
| μ | 1.39 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 2.00 | debye | KDB |
| ΔfG° | -42.55 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-163.00; -162.80] | kJ/mol |
|
| ΔfH°gas | -162.88 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -162.80 | kJ/mol | KDB |
| ΔfH°gas | -163.00 ± 0.75 | kJ/mol | NIST |
| ΔfH°liquid | -228.80 ± 1.40 | kJ/mol | NIST |
| ΔfusH° | 15.91 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [48.53; 65.90] | kJ/mol |
|
| ΔvapH° | 64.96 | kJ/mol | NIST |
| ΔvapH° | 64.60 | kJ/mol | NIST |
| ΔvapH° | 65.90 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 65.80 | kJ/mol | NIST |
| ΔvapH° | 48.53 | kJ/mol | NIST |
| IE | [8.00; 8.18] | eV |
|
| IE | 8.00 | eV | NIST |
| IE | 8.18 | eV | NIST |
| log10WS | [-1.19; -1.19] |
|
|
| log10WS | -1.19 | Aq. Solubility Prediction | |
| log10WS | -1.19 | Estimated Solubility | |
| logPoct/wat | 2.009 | Crippen Calculated Property | |
| McVol | 105.690 | ml/mol | McGowan Calculated Property |
| Pc | [4356.98; 10132.50] | kPa |
|
| Pc | 4356.98 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4356.98 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 10132.50 ± 0.50 | kPa | NIST |
| Ptriple | 0.01 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [190.90; 1181.00] |
|
|
| Inp | 1124.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1094.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1128.00 | NIST | |
| Inp | 1162.00 | NIST | |
| Inp | 1177.00 | NIST | |
| Inp | 1134.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1133.00 | NIST | |
| Inp | 1135.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1148.90 | NIST | |
| Inp | 1150.10 | NIST | |
| Inp | 1151.40 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1172.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1145.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1154.00 | NIST | |
| Inp | 1156.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1134.00 | NIST | |
| Inp | 1149.00 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1134.00 | NIST | |
| Inp | Outlier 192.24 | NIST | |
| Inp | Outlier 190.90 | NIST | |
| Inp | Outlier 191.20 | NIST | |
| Inp | Outlier 192.69 | NIST | |
| Inp | 1144.00 | NIST | |
| Inp | 1120.00 | NIST | |
| Inp | 1123.00 | NIST | |
| Inp | 1134.00 | NIST | |
| Inp | Outlier 192.24 | NIST | |
| Ip | [2070.00; 2127.00] |
|
|
| Ip | 2087.00 | NIST | |
| Ip | 2078.00 | NIST | |
| Ip | 2073.00 | NIST | |
| Ip | 2090.00 | NIST | |
| Ip | 2098.99 | NIST | |
| Ip | 2094.74 | NIST | |
| Ip | 2098.02 | NIST | |
| Ip | 2098.97 | NIST | |
| Ip | 2079.00 | NIST | |
| Ip | 2070.00 | NIST | |
| Ip | 2078.00 | NIST | |
| Ip | Outlier 2127.00 | NIST | |
| Ip | 2078.00 | NIST | |
| Ip | 2098.02 | NIST | |
| Ip | 2070.00 | NIST | |
| Tboil | [483.15; 484.65] | K |
|
| Tboil | 484.08 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 484.13 | K | KDB |
| Tboil | 483.20 | K | NIST |
| Tboil | 483.15 ± 0.30 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 484.65 ± 1.00 | K | NIST |
| Tboil | 484.45 ± 2.00 | K | NIST |
| Tboil | 484.15 ± 3.00 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 483.15 ± 3.00 | K | NIST |
| Tc | [707.55; 818.15] | K |
|
| Tc | 707.60 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 707.60 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 707.55 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 707.60 | K | KDB |
| Tc | 707.55 ± 0.30 | K | NIST |
| Tc | Outlier 818.15 ± 2.00 | K | NIST |
| Tfus | [294.15; 300.15] | K |
|
| Tfus | 297.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 297.69 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 297.68 | K | KDB |
| Tfus | 297.65 | K | Aq. Solubility Prediction |
| Tfus | 299.00 | K | NIST |
| Tfus | 297.35 ± 0.20 | K | NIST |
| Tfus | 299.00 ± 0.20 | K | NIST |
| Tfus | 298.05 ± 0.20 | K | NIST |
| Tfus | 297.69 ± 0.05 | K | NIST |
| Tfus | 297.20 ± 0.50 | K | NIST |
| Tfus | 297.15 ± 3.00 | K | NIST |
| Tfus | 300.15 ± 2.00 | K | NIST |
| Tfus | 298.75 ± 1.00 | K | NIST |
| Tfus | Outlier 294.15 ± 3.00 | K | NIST |
| Tfus | 298.65 ± 2.00 | K | NIST |
| Tfus | 299.15 ± 2.00 | K | NIST |
| Tfus | 300.15 ± 2.00 | K | NIST |
| Ttriple | 297.68 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 3.82 | ChemSep v8.3 pure component data Compiled value | |
| URi | 5.02 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.387; 0.510] | m3/kmol |
|
| Vc | 0.387 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.510 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2920000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 12.76 | kJ/mol | 297.30 | NIST |
| ΔsubH | 61.50 ± 0.80 | kJ/mol | 310.00 | NIST |
| ΔvapH | [51.80; 65.90] | kJ/mol | [300.00; 457.50] |
|
| ΔvapH | 65.90 | kJ/mol | 300.00 | NIST |
| ΔvapH | 65.90 ± 0.20 | kJ/mol | 300.00 | NIST |
| ΔvapH | 65.90 ± 0.20 | kJ/mol | 300.00 | NIST |
| ΔvapH | 51.80 | kJ/mol | 457.50 | NIST |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 485.20 | K | 102.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [134.09; 388.83] | J/mol×K | [255.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 7.18220e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 6.09224e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 134.09 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 195.92 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 244.57 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 281.58 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 310.16 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 332.71 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 350.88 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 365.81 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 378.27 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 388.83 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [245.70; 325.90] | J/mol×K | [353.83; 523.83] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 7.87600e+01 | |||
| Coefficient B | 4.71800e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 353.83 | |||
| Temperature range, max. | 523.83 | |||
| Cp,liquid | 245.70 | J/mol×K | 353.83 | Calculated Property |
| Cp,liquid | 254.61 | J/mol×K | 372.72 | Calculated Property |
| Cp,liquid | 263.52 | J/mol×K | 391.61 | Calculated Property |
| Cp,liquid | 272.43 | J/mol×K | 410.50 | Calculated Property |
| Cp,liquid | 281.34 | J/mol×K | 429.39 | Calculated Property |
| Cp,liquid | 290.26 | J/mol×K | 448.27 | Calculated Property |
| Cp,liquid | 299.17 | J/mol×K | 467.16 | Calculated Property |
| Cp,liquid | 308.08 | J/mol×K | 486.05 | Calculated Property |
| Cp,liquid | 316.99 | J/mol×K | 504.94 | Calculated Property |
| Cp,liquid | 325.90 | J/mol×K | 523.83 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0146459; 0.0003264] | Pa×s | [297.68; 484.13] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -7.23530e+01 | |||
| Coefficient B | 6.08680e+03 | |||
| Coefficient C | 8.37110e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 484.13 | |||
| η | 0.0146459 | Pa×s | 297.68 | Calculated Property |
| η | 0.0068001 | Pa×s | 318.40 | Calculated Property |
| η | 0.0035849 | Pa×s | 339.11 | Calculated Property |
| η | 0.0020954 | Pa×s | 359.83 | Calculated Property |
| η | 0.0013330 | Pa×s | 380.55 | Calculated Property |
| η | 0.0009097 | Pa×s | 401.26 | Calculated Property |
| η | 0.0006584 | Pa×s | 421.98 | Calculated Property |
| η | 0.0005007 | Pa×s | 442.70 | Calculated Property |
| η | 0.0003971 | Pa×s | 463.41 | Calculated Property |
| η | 0.0003264 | Pa×s | 484.13 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [63.25; 0.00] | kJ/mol | [297.68; 707.55] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 8.08330e+01 | |||
| Coefficient B | 4.49360e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.07550e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 707.65 K. | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 707.55 | |||
| ΔvapH | 63.25 | kJ/mol | 297.68 | Calculated Property |
| ΔvapH | 59.99 | kJ/mol | 343.22 | Calculated Property |
| ΔvapH | 56.49 | kJ/mol | 388.76 | Calculated Property |
| ΔvapH | 52.71 | kJ/mol | 434.30 | Calculated Property |
| ΔvapH | 48.57 | kJ/mol | 479.84 | Calculated Property |
| ΔvapH | 43.93 | kJ/mol | 525.39 | Calculated Property |
| ΔvapH | 38.60 | kJ/mol | 570.93 | Calculated Property |
| ΔvapH | 32.17 | kJ/mol | 616.47 | Calculated Property |
| ΔvapH | 23.56 | kJ/mol | 662.01 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 707.55 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [367.30; 511.94] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54387e+01 | |||
| Coefficient B | -4.41754e+03 | |||
| Coefficient C | -7.57380e+01 | |||
| Temperature range, min. | 367.30 | |||
| Temperature range, max. | 511.94 | |||
| Pvap | 1.33 | kPa | 367.30 | Calculated Property |
| Pvap | 2.94 | kPa | 383.37 | Calculated Property |
| Pvap | 6.00 | kPa | 399.44 | Calculated Property |
| Pvap | 11.44 | kPa | 415.51 | Calculated Property |
| Pvap | 20.58 | kPa | 431.58 | Calculated Property |
| Pvap | 35.20 | kPa | 447.66 | Calculated Property |
| Pvap | 57.57 | kPa | 463.73 | Calculated Property |
| Pvap | 90.54 | kPa | 479.80 | Calculated Property |
| Pvap | 137.55 | kPa | 495.87 | Calculated Property |
| Pvap | 202.64 | kPa | 511.94 | Calculated Property |
| Pvap | [0.01; 4431.96] | kPa | [297.68; 707.55] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37452e+02 | |||
| Coefficient B | -1.25580e+04 | |||
| Coefficient C | -1.76110e+01 | |||
| Coefficient D | 8.49520e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 707.65 K. | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 707.55 | |||
| Pvap | 0.01 | kPa | 297.68 | Calculated Property |
| Pvap | 0.38 | kPa | 343.22 | Calculated Property |
| Pvap | 4.14 | kPa | 388.76 | Calculated Property |
| Pvap | 23.92 | kPa | 434.30 | Calculated Property |
| Pvap | 91.51 | kPa | 479.84 | Calculated Property |
| Pvap | 264.30 | kPa | 525.39 | Calculated Property |
| Pvap | 628.85 | kPa | 570.93 | Calculated Property |
| Pvap | 1308.49 | kPa | 616.47 | Calculated Property |
| Pvap | 2483.50 | kPa | 662.01 | Calculated Property |
| Pvap | 4431.96 | kPa | 707.55 | Calculated Property |
| Pvap | [0.42; 4394.54] | kPa | [345.71; 707.65] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.35548e+02 | |||
| Coefficient B | -1.25596e+04 | |||
| Coefficient C | -1.72828e+01 | |||
| Coefficient D | 7.98314e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 707.65 | |||
| Pvap | 0.42 | kPa | 345.71 | Calculated Property |
| Pvap | 3.53 | kPa | 385.93 | Calculated Property |
| Pvap | 17.83 | kPa | 426.14 | Calculated Property |
| Pvap | 63.47 | kPa | 466.36 | Calculated Property |
| Pvap | 176.15 | kPa | 506.57 | Calculated Property |
| Pvap | 408.60 | kPa | 546.79 | Calculated Property |
| Pvap | 832.02 | kPa | 587.00 | Calculated Property |
| Pvap | 1541.17 | kPa | 627.22 | Calculated Property |
| Pvap | 2666.26 | kPa | 667.43 | Calculated Property |
| Pvap | 4394.54 | kPa | 707.65 | Calculated Property |
| Pvap | [13.19; 104.94] | kPa | [417.53; 485.47] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42568e+01 | |||
| Coefficient B | -3.67387e+03 | |||
| Coefficient C | -1.02913e+02 | |||
| Reference | Andon, Biddiscombe, et al., 1960 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 417.53 | |||
| Temperature range, max. | 485.47 | |||
| Pvap | 13.19 | kPa | 417.53 | Calculated Property |
| Pvap | 17.34 | kPa | 425.08 | Calculated Property |
| Pvap | 22.52 | kPa | 432.63 | Calculated Property |
| Pvap | 28.90 | kPa | 440.18 | Calculated Property |
| Pvap | 36.68 | kPa | 447.73 | Calculated Property |
| Pvap | 46.08 | kPa | 455.27 | Calculated Property |
| Pvap | 57.35 | kPa | 462.82 | Calculated Property |
| Pvap | 70.73 | kPa | 470.37 | Calculated Property |
| Pvap | 86.49 | kPa | 477.92 | Calculated Property |
| Pvap | 104.94 | kPa | 485.47 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1014.95; 365.20] | kg/m3 | [297.68; 707.55] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 8.17228e+01 | |||
| Coefficient B | 2.60890e-01 | |||
| Coefficient C | 7.07650e+02 | |||
| Coefficient D | 2.44770e-01 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 707.65 K. | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 707.55 | |||
| ρl | 1014.95 | kg/m3 | 297.68 | Calculated Property |
| ρl | 981.61 | kg/m3 | 343.22 | Calculated Property |
| ρl | 946.22 | kg/m3 | 388.76 | Calculated Property |
| ρl | 908.28 | kg/m3 | 434.30 | Calculated Property |
| ρl | 867.06 | kg/m3 | 479.84 | Calculated Property |
| ρl | 821.41 | kg/m3 | 525.39 | Calculated Property |
| ρl | 769.32 | kg/m3 | 570.93 | Calculated Property |
| ρl | 706.76 | kg/m3 | 616.47 | Calculated Property |
| ρl | 622.60 | kg/m3 | 662.01 | Calculated Property |
| ρl | 365.20 | kg/m3 | 707.55 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [297.65; 484.15] |
Jasper (1972), surface tension of pure liquid compounds Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is γ in N/m, T in K | |||
| Coefficient A | 5.83067e-02 | |||
| Coefficient B | -8.69000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 297.65 | |||
| Temperature range, max. | 484.15 | |||
| γ | 0.03 | N/m | 297.65 | Calculated Property |
| γ | 0.03 | N/m | 318.37 | Calculated Property |
| γ | 0.03 | N/m | 339.09 | Calculated Property |
| γ | 0.03 | N/m | 359.82 | Calculated Property |
| γ | 0.03 | N/m | 380.54 | Calculated Property |
| γ | 0.02 | N/m | 401.26 | Calculated Property |
| γ | 0.02 | N/m | 421.98 | Calculated Property |
| γ | 0.02 | N/m | 442.71 | Calculated Property |
| γ | 0.02 | N/m | 463.43 | Calculated Property |
| γ | 0.02 | N/m | 484.15 | Calculated Property |
| γ | [0.03; 0.00] | N/m | [297.68; 707.55] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is γ in N/m, T in K | |||
| Coefficient A | 6.05450e-02 | |||
| Coefficient B | 1.13620e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.07550e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 707.65 K. | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 707.55 | |||
| γ | 0.03 | N/m | 297.68 | Calculated Property |
| γ | 0.03 | N/m | 343.22 | Calculated Property |
| γ | 0.02 | N/m | 388.76 | Calculated Property |
| γ | 0.02 | N/m | 434.30 | Calculated Property |
| γ | 0.02 | N/m | 479.84 | Calculated Property |
| γ | 0.01 | N/m | 525.39 | Calculated Property |
| γ | 0.01 | N/m | 570.93 | Calculated Property |
| γ | 0.01 | N/m | 616.47 | Calculated Property |
| γ | 0.00 | N/m | 662.01 | Calculated Property |
| γ | 0.00 | N/m | 707.55 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.07] | W/m×K | [484.13; 1000.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λgas in W/m×K, T in K | |||
| Coefficient A | 1.98700e-04 | |||
| Coefficient B | 9.32300e-01 | |||
| Coefficient C | 7.22690e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 484.13 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 484.13 | Calculated Property |
| λgas | 0.03 | W/m×K | 541.45 | Calculated Property |
| λgas | 0.03 | W/m×K | 598.77 | Calculated Property |
| λgas | 0.04 | W/m×K | 656.09 | Calculated Property |
| λgas | 0.05 | W/m×K | 713.41 | Calculated Property |
| λgas | 0.05 | W/m×K | 770.72 | Calculated Property |
| λgas | 0.06 | W/m×K | 828.04 | Calculated Property |
| λgas | 0.06 | W/m×K | 885.36 | Calculated Property |
| λgas | 0.07 | W/m×K | 942.68 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.16; 0.10] | W/m×K | [297.68; 562.29] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is λliquid in W/m×K, T in K | |||
| Coefficient A | 2.31920e-01 | |||
| Coefficient B | -2.37140e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 297.68 | |||
| Temperature range, max. | 562.29 | |||
| λliquid | 0.16 | W/m×K | 297.68 | Calculated Property |
| λliquid | 0.15 | W/m×K | 327.08 | Calculated Property |
| λliquid | 0.15 | W/m×K | 356.48 | Calculated Property |
| λliquid | 0.14 | W/m×K | 385.88 | Calculated Property |
| λliquid | 0.13 | W/m×K | 415.28 | Calculated Property |
| λliquid | 0.13 | W/m×K | 444.69 | Calculated Property |
| λliquid | 0.12 | W/m×K | 474.09 | Calculated Property |
| λliquid | 0.11 | W/m×K | 503.49 | Calculated Property |
| λliquid | 0.11 | W/m×K | 532.89 | Calculated Property |
| λliquid | 0.10 | W/m×K | 562.29 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2,4-dimethyl-.
Mixtures
Sources
- KDB Vapor Pressure Data
- Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) ChEDL chemicals 1.5.2, from Bradley, J.-C.; Williams, A.; Lang, A. Jean-Claude Bradley Open Melting Point Dataset. Figshare, 2014 (CC0).
- IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 ChEDL chemicals 1.5.2, from Kudchadker, A. P.; Ambrose, D.; Tsonopoulos, C. Vapor-Liquid Critical Properties of Elements and Compounds. 7. Oxygen Compounds Other Than Alkanols and Cycloalkanols. J. Chem. Eng. Data 2001, 46, 457-479.
- Jasper (1972), surface tension of pure liquid compounds ChEDL chemicals 1.5.2, from Jasper, J. J. The Surface Tension of Pure Liquid Compounds. J. Phys. Chem. Ref. Data 1972, 1, 841-1010 (as transcribed in Lange's Handbook).
- PSRK revision IV (2005), critical constants and acentric factors of 1000 components ChEDL chemicals 1.5.2, from Horstmann, S.; Jabłoniec, A.; Krafczyk, J.; Fischer, K.; Gmehling, J. PSRK Group Contribution Equation of State: Comprehensive Revision and Extension IV, Including Critical Constants and α-Function Parameters for 1000 Components. Fluid Phase Equilib. 2005, 227, 157-164.
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Liquid-Liquid Equilibrium Measurements for Model Systems Related to Catalytic Fast Pyrolysis of Biomass
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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