- InChI
- InChI=1S/C8H10O/c1-6-4-3-5-8(9)7(6)2/h3-5,9H,1-2H3
- InChI Key
- QWBBPBRQALCEIZ-UHFFFAOYSA-N
- Formula
- C8H10O
- SMILES
- Cc1cccc(O)c1C
- Molecular Weight1
- 122.16
- CAS
- 526-75-0
- Other Names
-
- 1,2-Dimethyl-3-hydroxybenzene
- 1-hydroxy-2,3-dimethylbenzene
- 2,3-Xylenol
- 2,3-dimethylphenol
- NSC 62011
- o-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).
- 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 | [0.5157; 0.5407] |
|
|
| ω | 0.5407 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.5157 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°solid | -4336.00 ± 0.92 | kJ/mol | NIST |
| μ | 1.25 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -33.55 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | [-157.30; -157.19] | kJ/mol |
|
| ΔfH°gas | -157.19 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -157.30 | kJ/mol | KDB |
| ΔfH°gas | -157.30 ± 1.10 | kJ/mol | NIST |
| ΔfH°solid | -241.30 ± 1.10 | kJ/mol | NIST |
| ΔfusH° | 15.91 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [59.40; 84.00] | kJ/mol |
|
| ΔsubH° | 84.00 ± 1.00 | kJ/mol | NIST |
| ΔsubH° | 84.00 | kJ/mol | NIST |
| ΔsubH° | 59.40 ± 0.80 | kJ/mol | NIST |
| ΔvapH° | 62.01 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.26 | eV | NIST |
| log10WS | -1.43 | 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 | 0.36 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [196.80; 1200.00] |
|
|
| Inp | 1150.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1160.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1159.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1190.60 | NIST | |
| Inp | 1178.90 | NIST | |
| Inp | 1180.10 | NIST | |
| Inp | 1182.20 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1200.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1151.00 | NIST | |
| Inp | 1166.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Inp | 1158.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | 1178.00 | NIST | |
| Inp | 1181.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | Outlier 198.03 | NIST | |
| Inp | Outlier 196.80 | NIST | |
| Inp | Outlier 198.95 | NIST | |
| Inp | Outlier 198.65 | NIST | |
| Inp | Outlier 198.95 | NIST | |
| Inp | 1150.00 | NIST | |
| Inp | 1143.00 | NIST | |
| Inp | 1132.00 | NIST | |
| Inp | 1169.00 | NIST | |
| Inp | Outlier 198.03 | NIST | |
| Inp | 1153.00 | NIST | |
| Inp | 1167.00 | NIST | |
| Ip | [2120.00; 2188.00] |
|
|
| Ip | 2155.00 | NIST | |
| Ip | 2143.00 | NIST | |
| Ip | 2137.00 | NIST | |
| Ip | 2140.00 | NIST | |
| Ip | 2147.00 | NIST | |
| Ip | 2147.00 | NIST | |
| Ip | 2120.00 | NIST | |
| Ip | Outlier 2188.00 | NIST | |
| Ip | 2147.00 | NIST | |
| Ip | 2155.00 | NIST | |
| Tboil | [484.65; 492.15] | K |
|
| Tboil | 491.15 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 490.07 | K | KDB |
| Tboil | 491.20 | K | NIST |
| Tboil | 491.20 ± 2.00 | K | NIST |
| Tboil | 491.15 ± 2.00 | K | NIST |
| Tboil | 490.95 ± 2.00 | K | NIST |
| Tboil | 490.25 ± 2.00 | K | NIST |
| Tboil | 492.15 ± 3.00 | K | NIST |
| Tboil | 491.15 ± 2.00 | K | NIST |
| Tboil | 491.15 ± 3.00 | K | NIST |
| Tboil | Outlier 484.65 ± 5.00 | K | NIST |
| Tc | [722.80; 722.85] | K |
|
| Tc | 722.80 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 722.80 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 722.85 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 722.80 | K | KDB |
| Tc | 722.85 ± 0.40 | K | NIST |
| Tfus | [345.45; 348.15] | K |
|
| Tfus | 345.65 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 345.72 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 345.90 | K | KDB |
| Tfus | 345.91 | K | Aq. Solubility Prediction |
| Tfus | 345.45 ± 0.20 | K | NIST |
| Tfus | 345.72 ± 0.05 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 345.95 ± 1.00 | K | NIST |
| Tfus | 347.85 ± 1.00 | K | NIST |
| Tfus | 346.65 ± 1.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 348.15 ± 2.00 | K | NIST |
| Tfus | 347.65 ± 2.00 | K | NIST |
| Ttriple | 345.71 | K | ChemSep v8.3 pure component data Compiled value |
| URi | 5.02 | ChemSep v8.3 pure component data Compiled value | |
| Vc | 0.387 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Zc | 0.2930000 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | [20.29; 21.02] | kJ/mol | [345.80; 346.00] |
|
| ΔfusH | 20.29 | kJ/mol | 345.80 | NIST |
| ΔfusH | 21.02 | kJ/mol | 346.00 | NIST |
| ΔfusH | 21.02 | kJ/mol | 346.00 | NIST |
| ΔfusH | 21.02 | kJ/mol | 346.00 | NIST |
| ΔsubH | [61.50; 84.00] | kJ/mol | [303.00; 310.00] |
|
| ΔsubH | 84.00 ± 1.00 | kJ/mol | 303.00 | NIST |
| ΔsubH | 61.50 ± 0.80 | kJ/mol | 310.00 | NIST |
| ΔvapH | 52.10 | kJ/mol | 462.50 | NIST |
| ΔfusS | 60.76 | J/mol×K | 346.00 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [144.13; 390.10] | 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 | 8.40000e+01 | |||
| Coefficient B | -5.00000e+02 | |||
| Coefficient C | 6.05724e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 255.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 144.13 | J/mol×K | 255.00 | Calculated Property |
| Cp,gas | 203.83 | J/mol×K | 393.33 | Calculated Property |
| Cp,gas | 250.80 | J/mol×K | 531.67 | Calculated Property |
| Cp,gas | 286.55 | J/mol×K | 670.00 | Calculated Property |
| Cp,gas | 314.14 | J/mol×K | 808.33 | Calculated Property |
| Cp,gas | 335.91 | J/mol×K | 946.67 | Calculated Property |
| Cp,gas | 353.46 | J/mol×K | 1085.00 | Calculated Property |
| Cp,gas | 367.87 | J/mol×K | 1223.33 | Calculated Property |
| Cp,gas | 379.91 | J/mol×K | 1361.67 | Calculated Property |
| Cp,gas | 390.10 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [251.33; 330.15] | J/mol×K | [361.48; 541.48] |
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 | 9.30400e+01 | |||
| Coefficient B | 4.37900e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 361.48 | |||
| Temperature range, max. | 541.48 | |||
| Cp,liquid | 251.33 | J/mol×K | 361.48 | Calculated Property |
| Cp,liquid | 260.09 | J/mol×K | 381.48 | Calculated Property |
| Cp,liquid | 268.85 | J/mol×K | 401.48 | Calculated Property |
| Cp,liquid | 277.61 | J/mol×K | 421.48 | Calculated Property |
| Cp,liquid | 286.36 | J/mol×K | 441.48 | Calculated Property |
| Cp,liquid | 295.12 | J/mol×K | 461.48 | Calculated Property |
| Cp,liquid | 303.88 | J/mol×K | 481.48 | Calculated Property |
| Cp,liquid | 312.64 | J/mol×K | 501.48 | Calculated Property |
| Cp,liquid | 321.40 | J/mol×K | 521.48 | Calculated Property |
| Cp,liquid | 330.15 | J/mol×K | 541.48 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0028203; 0.0002929] | Pa×s | [345.71; 490.07] |
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 | -6.40380e+01 | |||
| Coefficient B | 5.59840e+03 | |||
| Coefficient C | 7.18030e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 490.07 | |||
| η | 0.0028203 | Pa×s | 345.71 | Calculated Property |
| η | 0.0019049 | Pa×s | 361.75 | Calculated Property |
| η | 0.0013484 | Pa×s | 377.79 | Calculated Property |
| η | 0.0009939 | Pa×s | 393.83 | Calculated Property |
| η | 0.0007590 | Pa×s | 409.87 | Calculated Property |
| η | 0.0005978 | Pa×s | 425.91 | Calculated Property |
| η | 0.0004838 | Pa×s | 441.95 | Calculated Property |
| η | 0.0004010 | Pa×s | 457.99 | Calculated Property |
| η | 0.0003395 | Pa×s | 474.03 | Calculated Property |
| η | 0.0002929 | Pa×s | 490.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [57.66; 0.00] | kJ/mol | [345.71; 722.85] |
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 | 7.20270e+01 | |||
| Coefficient B | 3.41940e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.22850e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 722.95 K. | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 722.85 | |||
| ΔvapH | 57.66 | kJ/mol | 345.71 | Calculated Property |
| ΔvapH | 55.38 | kJ/mol | 387.61 | Calculated Property |
| ΔvapH | 52.91 | kJ/mol | 429.52 | Calculated Property |
| ΔvapH | 50.20 | kJ/mol | 471.42 | Calculated Property |
| ΔvapH | 47.16 | kJ/mol | 513.33 | Calculated Property |
| ΔvapH | 43.70 | kJ/mol | 555.23 | Calculated Property |
| ΔvapH | 39.60 | kJ/mol | 597.14 | Calculated Property |
| ΔvapH | 34.48 | kJ/mol | 639.04 | Calculated Property |
| ΔvapH | 27.20 | kJ/mol | 680.95 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 722.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.30; 202.64] | kPa | [345.71; 518.24] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.54381e+01 | |||
| Coefficient B | -4.46433e+03 | |||
| Coefficient C | -7.73890e+01 | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 518.24 | |||
| Pvap | 0.30 | kPa | 345.71 | Calculated Property |
| Pvap | 0.91 | kPa | 364.88 | Calculated Property |
| Pvap | 2.41 | kPa | 384.05 | Calculated Property |
| Pvap | 5.68 | kPa | 403.22 | Calculated Property |
| Pvap | 12.16 | kPa | 422.39 | Calculated Property |
| Pvap | 24.03 | kPa | 441.56 | Calculated Property |
| Pvap | 44.35 | kPa | 460.73 | Calculated Property |
| Pvap | 77.23 | kPa | 479.90 | Calculated Property |
| Pvap | 127.88 | kPa | 499.07 | Calculated Property |
| Pvap | 202.64 | kPa | 518.24 | Calculated Property |
| Pvap | [0.36; 4932.30] | kPa | [345.71; 722.85] |
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 | 1.19782e+02 | |||
| Coefficient B | -1.17550e+04 | |||
| Coefficient C | -1.49920e+01 | |||
| Coefficient D | 7.04040e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 722.95 K. | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 722.85 | |||
| Pvap | 0.36 | kPa | 345.71 | Calculated Property |
| Pvap | 3.19 | kPa | 387.61 | Calculated Property |
| Pvap | 16.81 | kPa | 429.52 | Calculated Property |
| Pvap | 61.85 | kPa | 471.42 | Calculated Property |
| Pvap | 176.63 | kPa | 513.33 | Calculated Property |
| Pvap | 420.36 | kPa | 555.23 | Calculated Property |
| Pvap | 876.55 | kPa | 597.14 | Calculated Property |
| Pvap | 1660.31 | kPa | 639.04 | Calculated Property |
| Pvap | 2933.58 | kPa | 680.95 | Calculated Property |
| Pvap | 4932.30 | kPa | 722.85 | Calculated Property |
| Pvap | [0.45; 5077.93] | kPa | [345.71; 722.95] |
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 | 1.05582e+02 | |||
| Coefficient B | -1.07419e+04 | |||
| Coefficient C | -1.30204e+01 | |||
| Coefficient D | 6.74763e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 722.95 | |||
| Pvap | 0.45 | kPa | 345.71 | Calculated Property |
| Pvap | 3.60 | kPa | 387.63 | Calculated Property |
| Pvap | 17.82 | kPa | 429.54 | Calculated Property |
| Pvap | 63.18 | kPa | 471.46 | Calculated Property |
| Pvap | 176.96 | kPa | 513.37 | Calculated Property |
| Pvap | 418.09 | kPa | 555.29 | Calculated Property |
| Pvap | 872.96 | kPa | 597.20 | Calculated Property |
| Pvap | 1665.71 | kPa | 639.12 | Calculated Property |
| Pvap | 2977.22 | kPa | 681.03 | Calculated Property |
| Pvap | 5077.93 | kPa | 722.95 | Calculated Property |
| Pvap | [11.88; 104.11] | kPa | [422.50; 491.62] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.01422e+01 | |||
| Coefficient B | -1.34185e+03 | |||
| Coefficient C | -2.47500e+02 | |||
| Reference | Andon, Biddiscombe, et al., 1960 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 422.50 | |||
| Temperature range, max. | 491.62 | |||
| Pvap | 11.88 | kPa | 422.50 | Calculated Property |
| Pvap | 16.39 | kPa | 430.18 | Calculated Property |
| Pvap | 22.05 | kPa | 437.86 | Calculated Property |
| Pvap | 28.98 | kPa | 445.54 | Calculated Property |
| Pvap | 37.32 | kPa | 453.22 | Calculated Property |
| Pvap | 47.19 | kPa | 460.90 | Calculated Property |
| Pvap | 58.71 | kPa | 468.58 | Calculated Property |
| Pvap | 71.98 | kPa | 476.26 | Calculated Property |
| Pvap | 87.09 | kPa | 483.94 | Calculated Property |
| Pvap | 104.11 | kPa | 491.62 | Calculated Property |
| Pvap | [1.31; 104.59] | kPa | [357.00; 492.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.53140e+01 | |||
| Coefficient B | -4.94437e+03 | |||
| Coefficient C | -2.83470e+01 | |||
| Reference | von Terres, Gebert, et al., 1955 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 357.00 | |||
| Temperature range, max. | 492.00 | |||
| Pvap | 1.31 | kPa | 357.00 | Calculated Property |
| Pvap | 2.53 | kPa | 372.00 | Calculated Property |
| Pvap | 4.61 | kPa | 387.00 | Calculated Property |
| Pvap | 8.02 | kPa | 402.00 | Calculated Property |
| Pvap | 13.36 | kPa | 417.00 | Calculated Property |
| Pvap | 21.43 | kPa | 432.00 | Calculated Property |
| Pvap | 33.24 | kPa | 447.00 | Calculated Property |
| Pvap | 50.02 | kPa | 462.00 | Calculated Property |
| Pvap | 73.22 | kPa | 477.00 | Calculated Property |
| Pvap | 104.59 | kPa | 492.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [942.00; 374.48] | kg/m3 | [345.71; 722.85] |
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 | 9.95869e+01 | |||
| Coefficient B | 2.93000e-01 | |||
| Coefficient C | 7.22950e+02 | |||
| Coefficient D | 2.85710e-01 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 722.95 K. | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 722.85 | |||
| ρl | 942.00 | kg/m3 | 345.71 | Calculated Property |
| ρl | 910.76 | kg/m3 | 387.61 | Calculated Property |
| ρl | 877.78 | kg/m3 | 429.52 | Calculated Property |
| ρl | 842.63 | kg/m3 | 471.42 | Calculated Property |
| ρl | 804.70 | kg/m3 | 513.33 | Calculated Property |
| ρl | 763.00 | kg/m3 | 555.23 | Calculated Property |
| ρl | 715.87 | kg/m3 | 597.14 | Calculated Property |
| ρl | 659.90 | kg/m3 | 639.04 | Calculated Property |
| ρl | 585.86 | kg/m3 | 680.95 | Calculated Property |
| ρl | 374.48 | kg/m3 | 722.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [345.71; 722.85] |
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 | 6.07000e-02 | |||
| Coefficient B | 1.15280e+00 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 7.22850e+02 | |||
| Comment | Range stopped at Tc; ChemSep gives it to 722.95 K. | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 722.85 | |||
| γ | 0.03 | N/m | 345.71 | Calculated Property |
| γ | 0.03 | N/m | 387.61 | Calculated Property |
| γ | 0.02 | N/m | 429.52 | Calculated Property |
| γ | 0.02 | N/m | 471.42 | Calculated Property |
| γ | 0.01 | N/m | 513.33 | Calculated Property |
| γ | 0.01 | N/m | 555.23 | Calculated Property |
| γ | 0.01 | N/m | 597.14 | Calculated Property |
| γ | 0.01 | N/m | 639.04 | Calculated Property |
| γ | 0.00 | N/m | 680.95 | Calculated Property |
| γ | 0.00 | N/m | 722.85 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.03; 0.07] | W/m×K | [490.07; 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 | 2.24500e-04 | |||
| Coefficient B | 9.15900e-01 | |||
| Coefficient C | 7.25030e+02 | |||
| Coefficient D | 0.00000e+00 | |||
| Temperature range, min. | 490.07 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.03 | W/m×K | 490.07 | Calculated Property |
| λgas | 0.03 | W/m×K | 546.73 | Calculated Property |
| λgas | 0.04 | W/m×K | 603.39 | Calculated Property |
| λgas | 0.04 | W/m×K | 660.05 | Calculated Property |
| λgas | 0.05 | W/m×K | 716.71 | Calculated Property |
| λgas | 0.05 | W/m×K | 773.36 | Calculated Property |
| λgas | 0.06 | W/m×K | 830.02 | Calculated Property |
| λgas | 0.06 | W/m×K | 886.68 | Calculated Property |
| λgas | 0.07 | W/m×K | 943.34 | 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 | [345.71; 576.89] |
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 | 2.35670e-01 | |||
| Coefficient B | -2.37110e-04 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 345.71 | |||
| Temperature range, max. | 576.89 | |||
| λliquid | 0.15 | W/m×K | 345.71 | Calculated Property |
| λliquid | 0.15 | W/m×K | 371.40 | Calculated Property |
| λliquid | 0.14 | W/m×K | 397.08 | Calculated Property |
| λliquid | 0.14 | W/m×K | 422.77 | Calculated Property |
| λliquid | 0.13 | W/m×K | 448.46 | Calculated Property |
| λliquid | 0.12 | W/m×K | 474.14 | Calculated Property |
| λliquid | 0.12 | W/m×K | 499.83 | Calculated Property |
| λliquid | 0.11 | W/m×K | 525.52 | Calculated Property |
| λliquid | 0.10 | W/m×K | 551.20 | Calculated Property |
| λliquid | 0.10 | W/m×K | 576.89 | Calculated Property |
Similar Compounds
Find more compounds similar to Phenol, 2,3-dimethyl-.
Mixtures
- Phenol, 2,3-dimethyl- + Carbon dioxide
- Methyl Isobutyl Ketone + Phenol, 2,3-dimethyl- + Water
- Phenol, 2,3-dimethyl- + Choline chloride
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.
- 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
- Experiments and COSMO-SAC Modeling of Methyl Isobutyl Ketone + Dimethylphenols + Water Mixtures
- Solubilities of Substituted Phenols in Supercritical Carbon Dioxide
- Formation of Deep Eutectic Solvents by Phenols and Choline Chloride and Their Physical Properties
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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