- InChI
- InChI=1S/C8H10O/c1-6-3-4-7(2)8(9)5-6/h3-5,9H,1-2H3
- InChI Key
- NKTOLZVEWDHZMU-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- Cc1ccc(C)c(O)c1
- Molecular Weight1
- 122.16
- CAS
- 95-87-4
- Other Names
-
- 1,2,5-Xylenol
- 1,4-Dimethyl-2-hydroxybenzene
- 1-hydroxy-2,5-dimethylbenzene
- 2,5-Dmp
- 2,5-dimethylphenol
- 2,5-xylenol
- 2-Hydroxy-p-xylene
- 3,6-Dimethylphenol
- 3,6-Xylenol
- 6-Methyl-m-cresol
- NSC 2599
- p-Xylenol
- ω : Acentric Factor.
- ΔcH°solid : Standard solid 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°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).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- Ip : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (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 | [0.5474; 0.5638] |
|
|
| ω | 0.5474 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5638 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | -4330.61 ± 0.92 | kJ/mol | NIST |
| μ | [1.43; 1.50] | debye |
|
| μ | 1.43 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 1.50 | debye | KDB |
| ΔfG° | -39.67 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-161.70; -161.50] | kJ/mol |
|
| ΔfH°gas | -161.63 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -161.50 | kJ/mol | KDB |
| ΔfH°gas | -161.70 ± 0.50 | kJ/mol | NIST |
| ΔfH°solid | -246.30 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 15.91 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [84.60; 85.00] | kJ/mol |
|
| ΔsubH° | 85.00 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 84.60 | kJ/mol | NIST |
| ΔvapH° | 67.48 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.03 | eV | Relay (1.0) Calculated Property |
| log10WS | -1.54 | Aq. Solubility Prediction | |
| logPoct/wat | 2.009 | Crippen Calculated Property | |
| McVol | 105.690 | ml/mol | McGowan Calculated Property |
| Pc | [4863.60; 4863.60] | kPa |
|
| Pc | 4863.60 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 4863.60 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 0.56 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [190.90; 1174.00] |
|
|
| Inp | 1124.80 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1130.00 | NIST | |
| Inp | 1140.00 | NIST | |
| Inp | 1161.00 | NIST | |
| Inp | 1124.80 | NIST | |
| Inp | 1108.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1150.90 | NIST | |
| Inp | 1151.80 | NIST | |
| Inp | 1153.50 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1126.00 | NIST | |
| Inp | 1127.00 | NIST | |
| Inp | 1122.00 | NIST | |
| Inp | 1148.00 | NIST | |
| Inp | 1109.00 | NIST | |
| Inp | 1170.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | Outlier 192.82 | NIST | |
| Inp | Outlier 190.90 | NIST | |
| Inp | Outlier 192.94 | NIST | |
| Inp | 1150.90 | NIST | |
| Inp | 1125.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Ip | [2066.00; 2086.00] |
|
|
| Ip | 2072.00 | NIST | |
| Ip | 2085.00 | NIST | |
| Ip | 2074.00 | NIST | |
| Ip | 2073.00 | NIST | |
| Ip | 2086.00 | NIST | |
| Ip | 2072.00 | NIST | |
| Ip | 2066.00 | NIST | |
| Ip | 2068.00 | NIST | |
| Ip | 2074.00 | NIST | |
| Ip | 2072.00 | NIST | |
| Tboil | [483.15; 484.70] | K |
|
| Tboil | 484.28 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 484.33 | K | KDB |
| Tboil | 484.70 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 484.50 ± 2.00 | K | NIST |
| Tboil | 484.65 ± 2.00 | K | NIST |
| Tboil | 484.35 ± 2.00 | K | NIST |
| Tboil | 483.15 ± 2.00 | K | NIST |
| Tboil | 483.15 ± 3.00 | K | NIST |
| Tboil | 483.15 ± 3.00 | K | NIST |
| Tc | [706.90; 723.05] | K |
|
| Tc | 706.90 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 706.90 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 723.05 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 706.90 | K | KDB |
| Tc | 706.90 ± 0.20 | K | NIST |
| Tc | 723.05 ± 0.50 | K | NIST |
| Tfus | [347.15; 348.65] | K |
|
| Tfus | 347.95 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 348.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 347.90 | K | KDB |
| Tfus | 348.27 | K | Aq. Solubility Prediction |
| Tfus | 347.65 ± 0.20 | K | NIST |
| Tfus | 348.00 ± 0.05 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 0.50 | K | NIST |
| Tfus | Outlier 348.65 ± 1.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 347.65 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 347.65 ± 2.00 | K | NIST |
| Tfus | Outlier 347.15 ± 2.00 | K | NIST |
| Tfus | Outlier 347.15 ± 2.00 | K | NIST |
| Tfus | 347.65 ± 2.00 | K | NIST |
| Tfus | 347.65 ± 2.00 | K | NIST |
| Ttriple | 347.99 | 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 | [0.350; 0.470] | m3/kmol |
|
| Vc | 0.350 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.470 | 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 | [13.81; 23.38] | kJ/mol | [348.00; 348.10] |
|
| ΔfusH | 23.38 | kJ/mol | 348.00 | NIST |
| ΔfusH | 23.38 | kJ/mol | 348.00 | NIST |
| ΔfusH | 23.38 | kJ/mol | 348.00 | NIST |
| ΔfusH | 13.81 | kJ/mol | 348.10 | NIST |
| ΔsubH | [64.00; 85.00] | kJ/mol | [302.50; 348.00] |
|
| ΔsubH | 85.00 ± 0.25 | kJ/mol | 302.50 | NIST |
| ΔsubH | 64.00 ± 0.80 | kJ/mol | 348.00 | NIST |
| ΔvapH | 51.70 | kJ/mol | 456.00 | NIST |
| ΔfusS | 67.17 | J/mol×K | 348.00 | 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 | [237.96; 316.70] | J/mol×K | [353.53; 523.53] |
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 | 7.42000e+01 | |||
| Coefficient B | 4.63200e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 353.53 | |||
| Temperature range, max. | 523.53 | |||
| Cp,liquid | 237.96 | J/mol×K | 353.53 | Calculated Property |
| Cp,liquid | 246.70 | J/mol×K | 372.42 | Calculated Property |
| Cp,liquid | 255.45 | J/mol×K | 391.31 | Calculated Property |
| Cp,liquid | 264.20 | J/mol×K | 410.20 | Calculated Property |
| Cp,liquid | 272.95 | J/mol×K | 429.09 | Calculated Property |
| Cp,liquid | 281.70 | J/mol×K | 447.97 | Calculated Property |
| Cp,liquid | 290.45 | J/mol×K | 466.86 | Calculated Property |
| Cp,liquid | 299.20 | J/mol×K | 485.75 | Calculated Property |
| Cp,liquid | 307.95 | J/mol×K | 504.64 | Calculated Property |
| Cp,liquid | 316.70 | J/mol×K | 523.53 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0015269; 0.0002938] | Pa×s | [347.99; 484.33] |
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 | -1.69070e+01 | |||
| Coefficient B | 2.30310e+03 | |||
| Coefficient C | 6.50050e-01 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 484.33 | |||
| η | 0.0015269 | Pa×s | 347.99 | Calculated Property |
| η | 0.0011911 | Pa×s | 363.14 | Calculated Property |
| η | 0.0009488 | Pa×s | 378.29 | Calculated Property |
| η | 0.0007699 | Pa×s | 393.44 | Calculated Property |
| η | 0.0006351 | Pa×s | 408.59 | Calculated Property |
| η | 0.0005316 | Pa×s | 423.73 | Calculated Property |
| η | 0.0004509 | Pa×s | 438.88 | Calculated Property |
| η | 0.0003869 | Pa×s | 454.03 | Calculated Property |
| η | 0.0003355 | Pa×s | 469.18 | Calculated Property |
| η | 0.0002938 | Pa×s | 484.33 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [56.64; 21.47] | kJ/mol | [347.99; 707.05] |
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 | 6.93070e+01 | |||
| Coefficient B | 3.07480e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.23050e+02 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 707.05 | |||
| ΔvapH | 56.64 | kJ/mol | 347.99 | Calculated Property |
| ΔvapH | 54.71 | kJ/mol | 387.89 | Calculated Property |
| ΔvapH | 52.62 | kJ/mol | 427.78 | Calculated Property |
| ΔvapH | 50.33 | kJ/mol | 467.68 | Calculated Property |
| ΔvapH | 47.77 | kJ/mol | 507.57 | Calculated Property |
| ΔvapH | 44.85 | kJ/mol | 547.47 | Calculated Property |
| ΔvapH | 41.43 | kJ/mol | 587.36 | Calculated Property |
| ΔvapH | 37.23 | kJ/mol | 627.26 | Calculated Property |
| ΔvapH | 31.54 | kJ/mol | 667.15 | Calculated Property |
| ΔvapH | 21.47 | kJ/mol | 707.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.45; 202.66] | kPa | [347.99; 511.89] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54574e+01 | |||
| Coefficient B | -4.42459e+03 | |||
| Coefficient C | -7.57940e+01 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 511.89 | |||
| Pvap | 0.45 | kPa | 347.99 | Calculated Property |
| Pvap | 1.25 | kPa | 366.20 | Calculated Property |
| Pvap | 3.07 | kPa | 384.41 | Calculated Property |
| Pvap | 6.82 | kPa | 402.62 | Calculated Property |
| Pvap | 13.93 | kPa | 420.83 | Calculated Property |
| Pvap | 26.49 | kPa | 439.05 | Calculated Property |
| Pvap | 47.39 | kPa | 457.26 | Calculated Property |
| Pvap | 80.39 | kPa | 475.47 | Calculated Property |
| Pvap | 130.24 | kPa | 493.68 | Calculated Property |
| Pvap | 202.66 | kPa | 511.89 | Calculated Property |
| Pvap | [0.56; 4923.62] | kPa | [347.99; 707.05] |
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 | 5.53542e+01 | |||
| Coefficient B | -8.58000e+03 | |||
| Coefficient C | -5.34520e+00 | |||
| Coefficient D | 2.82440e-18 | |||
| Coefficient E | 6.00000e+00 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 707.05 | |||
| Pvap | 0.56 | kPa | 347.99 | Calculated Property |
| Pvap | 3.99 | kPa | 387.89 | Calculated Property |
| Pvap | 18.73 | kPa | 427.78 | Calculated Property |
| Pvap | 65.15 | kPa | 467.68 | Calculated Property |
| Pvap | 181.25 | kPa | 507.57 | Calculated Property |
| Pvap | 426.25 | kPa | 547.47 | Calculated Property |
| Pvap | 883.13 | kPa | 587.36 | Calculated Property |
| Pvap | 1664.63 | kPa | 627.26 | Calculated Property |
| Pvap | 2929.98 | kPa | 667.15 | Calculated Property |
| Pvap | 4923.62 | kPa | 707.05 | Calculated Property |
| Pvap | [0.51; 4959.92] | kPa | [347.99; 707.05] |
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 | 1.27627e+02 | |||
| Coefficient B | -1.20343e+04 | |||
| Coefficient C | -1.61842e+01 | |||
| Coefficient D | 8.17909e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 707.05 | |||
| Pvap | 0.51 | kPa | 347.99 | Calculated Property |
| Pvap | 3.91 | kPa | 387.89 | Calculated Property |
| Pvap | 18.88 | kPa | 427.78 | Calculated Property |
| Pvap | 65.82 | kPa | 467.68 | Calculated Property |
| Pvap | 181.78 | kPa | 507.57 | Calculated Property |
| Pvap | 424.23 | kPa | 547.47 | Calculated Property |
| Pvap | 875.91 | kPa | 587.36 | Calculated Property |
| Pvap | 1654.38 | kPa | 627.26 | Calculated Property |
| Pvap | 2930.40 | kPa | 667.15 | Calculated Property |
| Pvap | 4959.92 | kPa | 707.05 | Calculated Property |
| Pvap | [13.00; 102.87] | kPa | [417.07; 484.89] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41114e+01 | |||
| Coefficient B | -3.58796e+03 | |||
| Coefficient C | -1.06330e+02 | |||
| Reference | Andon, Biddiscombe, et al., 1960 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 417.07 | |||
| Temperature range, max. | 484.89 | |||
| Pvap | 13.00 | kPa | 417.07 | Calculated Property |
| Pvap | 17.09 | kPa | 424.61 | Calculated Property |
| Pvap | 22.18 | kPa | 432.14 | Calculated Property |
| Pvap | 28.44 | kPa | 439.68 | Calculated Property |
| Pvap | 36.08 | kPa | 447.21 | Calculated Property |
| Pvap | 45.31 | kPa | 454.75 | Calculated Property |
| Pvap | 56.35 | kPa | 462.28 | Calculated Property |
| Pvap | 69.44 | kPa | 469.82 | Calculated Property |
| Pvap | 84.86 | kPa | 477.35 | Calculated Property |
| Pvap | 102.87 | kPa | 484.89 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [967.38; 349.06] | kg/m3 | [347.99; 707.05] |
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 | 1.02712e+02 | |||
| Coefficient B | 2.94250e-01 | |||
| Coefficient C | 7.07050e+02 | |||
| Coefficient D | 2.69210e-01 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 707.05 | |||
| ρl | 967.38 | kg/m3 | 347.99 | Calculated Property |
| ρl | 937.09 | kg/m3 | 387.89 | Calculated Property |
| ρl | 904.97 | kg/m3 | 427.78 | Calculated Property |
| ρl | 870.60 | kg/m3 | 467.68 | Calculated Property |
| ρl | 833.31 | kg/m3 | 507.57 | Calculated Property |
| ρl | 792.09 | kg/m3 | 547.47 | Calculated Property |
| ρl | 745.17 | kg/m3 | 587.36 | Calculated Property |
| ρl | 688.96 | kg/m3 | 627.26 | Calculated Property |
| ρl | 613.66 | kg/m3 | 667.15 | Calculated Property |
| ρl | 349.06 | kg/m3 | 707.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.02] | N/m | [347.65; 484.65] |
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 | 5.99377e-02 | |||
| Coefficient B | -8.50000e-05 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 347.65 | |||
| Temperature range, max. | 484.65 | |||
| γ | 0.03 | N/m | 347.65 | Calculated Property |
| γ | 0.03 | N/m | 362.87 | Calculated Property |
| γ | 0.03 | N/m | 378.09 | Calculated Property |
| γ | 0.03 | N/m | 393.32 | Calculated Property |
| γ | 0.03 | N/m | 408.54 | Calculated Property |
| γ | 0.02 | N/m | 423.76 | Calculated Property |
| γ | 0.02 | N/m | 438.98 | Calculated Property |
| γ | 0.02 | N/m | 454.21 | Calculated Property |
| γ | 0.02 | N/m | 469.43 | Calculated Property |
| γ | 0.02 | N/m | 484.65 | Calculated Property |
| γ | [0.03; 0.00] | N/m | [347.99; 707.05] |
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 | 6.00580e-02 | |||
| Coefficient B | 1.00670e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.23050e+02 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 707.05 | |||
| γ | 0.03 | N/m | 347.99 | Calculated Property |
| γ | 0.03 | N/m | 387.89 | Calculated Property |
| γ | 0.02 | N/m | 427.78 | Calculated Property |
| γ | 0.02 | N/m | 467.68 | Calculated Property |
| γ | 0.02 | N/m | 507.57 | Calculated Property |
| γ | 0.01 | N/m | 547.47 | Calculated Property |
| γ | 0.01 | N/m | 587.36 | Calculated Property |
| γ | 0.01 | N/m | 627.26 | Calculated Property |
| γ | 0.00 | N/m | 667.15 | Calculated Property |
| γ | 0.00 | N/m | 707.05 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.07] | W/m×K | [484.33; 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 | 2.02610e-04 | |||
| Coefficient B | 9.29700e-01 | |||
| Coefficient C | 7.22680e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 484.33 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 484.33 | Calculated Property |
| λgas | 0.03 | W/m×K | 541.63 | Calculated Property |
| λgas | 0.04 | W/m×K | 598.92 | Calculated Property |
| λgas | 0.04 | W/m×K | 656.22 | Calculated Property |
| λgas | 0.05 | W/m×K | 713.52 | Calculated Property |
| λgas | 0.05 | W/m×K | 770.81 | Calculated Property |
| λgas | 0.06 | W/m×K | 828.11 | Calculated Property |
| λgas | 0.06 | W/m×K | 885.41 | Calculated Property |
| λgas | 0.07 | W/m×K | 942.70 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.15; 0.10] | W/m×K | [347.99; 562.11] |
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 | 2.33130e-01 | |||
| Coefficient B | -2.39670e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 347.99 | |||
| Temperature range, max. | 562.11 | |||
| λliquid | 0.15 | W/m×K | 347.99 | Calculated Property |
| λliquid | 0.14 | W/m×K | 371.78 | Calculated Property |
| λliquid | 0.14 | W/m×K | 395.57 | Calculated Property |
| λliquid | 0.13 | W/m×K | 419.36 | Calculated Property |
| λliquid | 0.13 | W/m×K | 443.15 | Calculated Property |
| λliquid | 0.12 | W/m×K | 466.95 | Calculated Property |
| λliquid | 0.12 | W/m×K | 490.74 | Calculated Property |
| λliquid | 0.11 | W/m×K | 514.53 | Calculated Property |
| λliquid | 0.10 | W/m×K | 538.32 | Calculated Property |
| λliquid | 0.10 | W/m×K | 562.11 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2,5-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.
- Cheméo Relay (1.0)
- 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
- Solubilities of Substituted Phenols in Supercritical Carbon Dioxide
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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