- InChI
- InChI=1S/C10H14/c1-4-10-7-8(2)5-6-9(10)3/h5-7H,4H2,1-3H3
- InChI Key
- AXIUBBVSOWPLDA-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCc1cc(C)ccc1C
- Molecular Weight1
- 134.22
- CAS
- 1758-88-9
- Other Names
-
- 1,4-Dimethyl-2-ethylbenzene
- 2,5-Dimethylethylbenzene
- 2-Ethyl p-xylene
- 2-Ethyl-1,4-dimethylbenzene
- 2-Ethyl-p-xylene
- p-Xylene, 2-ethyl-
- 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).
- 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).
- 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).
- 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.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3600; 0.4175] |
|
|
| ω | 0.4175 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3600 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3600 | KDB | |
| ΔcH°liquid | [-5851.10; -5850.70] | kJ/mol |
|
| ΔcH°liquid | -5851.10 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -5850.70 ± 2.60 | kJ/mol | NIST |
| ΔfG° | 127.30 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -32.18 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | [-85.30; -84.80] | kJ/mol |
|
| ΔfH°liquid | -84.80 ± 1.20 | kJ/mol | NIST |
| ΔfH°liquid | -85.30 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 14.92 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.60 | kJ/mol | NIST |
| IE | 8.17 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.77 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.866 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| Pc | [2899.92; 3380.00] | kPa |
|
| Pc | 2899.92 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 3380.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2900.00 | kPa | KDB |
| Ptriple | 7.49e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1049.00; 1093.00] |
|
|
| Inp | 1068.50 | NIST | |
| Inp | 1069.50 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1067.20 | NIST | |
| Inp | 1066.70 | NIST | |
| Inp | 1067.70 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | Outlier 1089.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1054.80 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1054.29 | NIST | |
| Inp | 1081.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | Outlier 1089.00 | NIST | |
| Inp | 1060.50 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1086.90 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | Outlier 1090.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1068.80 | NIST | |
| Inp | 1059.60 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1062.32 | NIST | |
| Inp | 1063.12 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | Outlier 1093.00 | NIST | |
| Inp | 1074.60 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | Outlier 1049.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1074.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1085.20 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1060.00 | NIST | |
| Inp | 1072.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1083.00 | NIST | |
| Inp | 1077.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1085.20 | NIST | |
| Inp | 1068.00 | NIST | |
| Ip | [1307.00; 1364.00] |
|
|
| Ip | 1307.00 | NIST | |
| Ip | 1343.50 | NIST | |
| Ip | 1335.00 | NIST | |
| Ip | 1321.10 | NIST | |
| Ip | 1339.00 | NIST | |
| Ip | Outlier 1364.00 | NIST | |
| Ip | 1321.00 | NIST | |
| Ip | 1323.00 | NIST | |
| Ip | 1341.00 | NIST | |
| Ip | 1344.00 | NIST | |
| Ip | 1321.00 | NIST | |
| Ip | 1344.00 | NIST | |
| Ip | 1307.00 | NIST | |
| Tboil | [459.00; 461.70] | K |
|
| Tboil | 460.09 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 460.10 | K | KDB |
| Tboil | 460.10 | K | NIST |
| Tboil | 459.98 ± 0.20 | K | NIST |
| Tboil | 459.60 ± 0.30 | K | NIST |
| Tboil | 459.60 ± 0.30 | K | NIST |
| Tboil | 460.06 ± 0.20 | K | NIST |
| Tboil | 459.60 ± 1.00 | K | NIST |
| Tboil | 459.60 ± 0.15 | K | NIST |
| Tboil | 460.40 ± 2.00 | K | NIST |
| Tboil | 460.06 ± 0.20 | K | NIST |
| Tboil | 459.60 ± 0.30 | K | NIST |
| Tboil | Outlier 461.70 ± 1.50 | K | NIST |
| Tboil | 459.00 ± 3.00 | K | NIST |
| Tc | [662.60; 680.00] | K |
|
| Tc | 662.60 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 680.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 662.60 | K | KDB |
| Tfus | [219.00; 219.50] | K |
|
| Tfus | 219.30 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 219.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 219.50 | K | KDB |
| Tfus | 219.41 ± 0.20 | K | NIST |
| Ttriple | 219.52 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.64 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.07 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.461; 0.461] | m3/kmol |
|
| Vc | 0.461 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.461 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.461 | m3/kmol | KDB |
| Zc | [0.2425620; 0.2520000] |
|
|
| Zc | 0.2520000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2425620 | KDB | |
| Zra | 0.27 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [48.00; 48.70] | kJ/mol | [369.50; 414.00] |
|
| ΔvapH | 48.70 | kJ/mol | 369.50 | NIST |
| ΔvapH | 48.00 | kJ/mol | 414.00 | NIST |
| ρl | 872.44 | kg/m3 | 293.10 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [165.28; 474.81] | J/mol×K | [273.00; 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 | 9.06930e+01 | |||
| Coefficient B | -5.33270e+02 | |||
| Coefficient C | 6.23124e+00 | |||
| Coefficient D | 1.41430e-04 | |||
| Coefficient E | -6.08630e-08 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 165.28 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 235.61 | J/mol×K | 409.33 | Calculated Property |
| Cp,gas | 293.65 | J/mol×K | 545.67 | Calculated Property |
| Cp,gas | 339.70 | J/mol×K | 682.00 | Calculated Property |
| Cp,gas | 376.29 | J/mol×K | 818.33 | Calculated Property |
| Cp,gas | 405.58 | J/mol×K | 954.67 | Calculated Property |
| Cp,gas | 429.12 | J/mol×K | 1091.00 | Calculated Property |
| Cp,gas | 448.02 | J/mol×K | 1227.33 | Calculated Property |
| Cp,gas | 463.06 | J/mol×K | 1363.67 | Calculated Property |
| Cp,gas | 474.81 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [247.84; 325.31] | J/mol×K | [298.15; 459.98] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.15180e+02 | |||
| Coefficient B | -6.91790e+01 | |||
| Coefficient C | 3.66624e+00 | |||
| Coefficient D | 6.51990e-03 | |||
| Coefficient E | -5.51640e-06 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 459.98 | |||
| Cp,liquid | 247.84 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 257.38 | J/mol×K | 316.13 | Calculated Property |
| Cp,liquid | 266.86 | J/mol×K | 334.11 | Calculated Property |
| Cp,liquid | 276.20 | J/mol×K | 352.09 | Calculated Property |
| Cp,liquid | 285.33 | J/mol×K | 370.07 | Calculated Property |
| Cp,liquid | 294.18 | J/mol×K | 388.06 | Calculated Property |
| Cp,liquid | 302.67 | J/mol×K | 406.04 | Calculated Property |
| Cp,liquid | 310.74 | J/mol×K | 424.02 | Calculated Property |
| Cp,liquid | 318.30 | J/mol×K | 442.00 | Calculated Property |
| Cp,liquid | 325.31 | J/mol×K | 459.98 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0067981; 0.0001021] | Pa×s | [219.52; 573.00] |
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 | -1.21390e+01 | |||
| Coefficient B | 1.50900e+03 | |||
| Coefficient C | 5.09950e-02 | |||
| Coefficient D | -2.35310e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 573.00 | |||
| η | 0.0067981 | Pa×s | 219.52 | Calculated Property |
| η | 0.0024142 | Pa×s | 258.80 | Calculated Property |
| η | 0.0011272 | Pa×s | 298.07 | Calculated Property |
| η | 0.0006288 | Pa×s | 337.35 | Calculated Property |
| η | 0.0003964 | Pa×s | 376.62 | Calculated Property |
| η | 0.0002727 | Pa×s | 415.90 | Calculated Property |
| η | 0.0002001 | Pa×s | 455.17 | Calculated Property |
| η | 0.0001543 | Pa×s | 494.45 | Calculated Property |
| η | 0.0001236 | Pa×s | 533.72 | Calculated Property |
| η | 0.0001021 | Pa×s | 573.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [53.01; 13.04] | kJ/mol | [219.52; 663.00] |
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 | 8.26994e+01 | |||
| Coefficient B | 2.58092e+00 | |||
| Coefficient C | -6.47610e+00 | |||
| Coefficient D | 7.12580e+00 | |||
| Coefficient E | -2.74032e+00 | |||
| Critical temperature, Tc (K) | 6.80000e+02 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 663.00 | |||
| ΔvapH | 53.01 | kJ/mol | 219.52 | Calculated Property |
| ΔvapH | 50.89 | kJ/mol | 268.80 | Calculated Property |
| ΔvapH | 48.99 | kJ/mol | 318.07 | Calculated Property |
| ΔvapH | 46.90 | kJ/mol | 367.35 | Calculated Property |
| ΔvapH | 44.31 | kJ/mol | 416.62 | Calculated Property |
| ΔvapH | 40.98 | kJ/mol | 465.90 | Calculated Property |
| ΔvapH | 36.72 | kJ/mol | 515.17 | Calculated Property |
| ΔvapH | 31.32 | kJ/mol | 564.45 | Calculated Property |
| ΔvapH | 24.31 | kJ/mol | 613.72 | Calculated Property |
| ΔvapH | 13.04 | kJ/mol | 663.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [336.42; 490.24] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47855e+01 | |||
| Coefficient B | -4.20569e+03 | |||
| Coefficient C | -4.63260e+01 | |||
| Temperature range, min. | 336.42 | |||
| Temperature range, max. | 490.24 | |||
| Pvap | 1.33 | kPa | 336.42 | Calculated Property |
| Pvap | 2.99 | kPa | 353.51 | Calculated Property |
| Pvap | 6.15 | kPa | 370.60 | Calculated Property |
| Pvap | 11.77 | kPa | 387.69 | Calculated Property |
| Pvap | 21.17 | kPa | 404.78 | Calculated Property |
| Pvap | 36.12 | kPa | 421.88 | Calculated Property |
| Pvap | 58.80 | kPa | 438.97 | Calculated Property |
| Pvap | 91.93 | kPa | 456.06 | Calculated Property |
| Pvap | 138.66 | kPa | 473.15 | Calculated Property |
| Pvap | 202.63 | kPa | 490.24 | Calculated Property |
| Pvap | [8.61e-05; 3299.60] | kPa | [219.52; 680.00] |
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 | 4.44502e+01 | |||
| Coefficient B | -7.09386e+03 | |||
| Coefficient C | -3.98884e+00 | |||
| Coefficient D | 2.14300e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 680.00 | |||
| Pvap | 8.61e-05 | kPa | 219.52 | Calculated Property |
| Pvap | 0.02 | kPa | 270.68 | Calculated Property |
| Pvap | 0.55 | kPa | 321.85 | Calculated Property |
| Pvap | 6.31 | kPa | 373.01 | Calculated Property |
| Pvap | 37.78 | kPa | 424.18 | Calculated Property |
| Pvap | 146.58 | kPa | 475.34 | Calculated Property |
| Pvap | 420.33 | kPa | 526.51 | Calculated Property |
| Pvap | 969.28 | kPa | 577.67 | Calculated Property |
| Pvap | 1901.55 | kPa | 628.84 | Calculated Property |
| Pvap | 3299.60 | kPa | 680.00 | Calculated Property |
| Pvap | [7.43e-05; 2847.62] | kPa | [219.52; 663.00] |
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 | 5.69470e+01 | |||
| Coefficient B | -7.63454e+03 | |||
| Coefficient C | -5.89162e+00 | |||
| Coefficient D | 1.81744e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 663.00 | |||
| Pvap | 7.43e-05 | kPa | 219.52 | Calculated Property |
| Pvap | 0.01 | kPa | 268.80 | Calculated Property |
| Pvap | 0.44 | kPa | 318.07 | Calculated Property |
| Pvap | 5.01 | kPa | 367.35 | Calculated Property |
| Pvap | 29.91 | kPa | 416.62 | Calculated Property |
| Pvap | 116.38 | kPa | 465.90 | Calculated Property |
| Pvap | 336.90 | kPa | 515.17 | Calculated Property |
| Pvap | 789.97 | kPa | 564.45 | Calculated Property |
| Pvap | 1588.21 | kPa | 613.72 | Calculated Property |
| Pvap | 2847.62 | kPa | 663.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [932.47; 467.00] | kg/m3 | [219.52; 639.66] |
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 | 2.09904e+01 | |||
| Coefficient B | 1.39570e-01 | |||
| Coefficient C | 6.80000e+02 | |||
| Coefficient D | 1.95660e-01 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 639.66 | |||
| ρl | 932.47 | kg/m3 | 219.52 | Calculated Property |
| ρl | 897.91 | kg/m3 | 266.20 | Calculated Property |
| ρl | 861.53 | kg/m3 | 312.88 | Calculated Property |
| ρl | 822.93 | kg/m3 | 359.57 | Calculated Property |
| ρl | 781.57 | kg/m3 | 406.25 | Calculated Property |
| ρl | 736.65 | kg/m3 | 452.93 | Calculated Property |
| ρl | 686.87 | kg/m3 | 499.61 | Calculated Property |
| ρl | 629.99 | kg/m3 | 546.30 | Calculated Property |
| ρl | 561.30 | kg/m3 | 592.98 | Calculated Property |
| ρl | 467.00 | kg/m3 | 639.66 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 4.35e-04] | N/m | [219.52; 663.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -2.54290e-02 | |||
| Coefficient B | 2.90010e+01 | |||
| Coefficient C | -2.56120e+00 | |||
| Coefficient D | -1.02500e-03 | |||
| Coefficient E | -1.04160e-06 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 663.00 | |||
| γ | 0.04 | N/m | 219.52 | Calculated Property |
| γ | 0.04 | N/m | 268.80 | Calculated Property |
| γ | 0.03 | N/m | 318.07 | Calculated Property |
| γ | 0.02 | N/m | 367.35 | Calculated Property |
| γ | 0.02 | N/m | 416.62 | Calculated Property |
| γ | 0.02 | N/m | 465.90 | Calculated Property |
| γ | 0.01 | N/m | 515.17 | Calculated Property |
| γ | 0.01 | N/m | 564.45 | Calculated Property |
| γ | 0.00 | N/m | 613.72 | Calculated Property |
| γ | 4.35e-04 | N/m | 663.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [219.52; 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 | 8.57320e-05 | |||
| Coefficient B | 1.04450e+00 | |||
| Coefficient C | 5.16180e+02 | |||
| Coefficient D | 4.66220e+04 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 219.52 | Calculated Property |
| λgas | 0.01 | W/m×K | 306.24 | Calculated Property |
| λgas | 0.02 | W/m×K | 392.96 | Calculated Property |
| λgas | 0.02 | W/m×K | 479.68 | Calculated Property |
| λgas | 0.03 | W/m×K | 566.40 | Calculated Property |
| λgas | 0.04 | W/m×K | 653.12 | Calculated Property |
| λgas | 0.05 | W/m×K | 739.84 | Calculated Property |
| λgas | 0.06 | W/m×K | 826.56 | Calculated Property |
| λgas | 0.07 | W/m×K | 913.28 | Calculated Property |
| λgas | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λliquid | [0.14; 0.09] | W/m×K | [219.52; 459.98] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λliquid in W/m×K, T in K | |||
| Coefficient A | -8.04490e-02 | |||
| Coefficient B | 4.79260e+00 | |||
| Coefficient C | -1.41910e+00 | |||
| Coefficient D | -3.20190e-04 | |||
| Coefficient E | -9.33680e-07 | |||
| Temperature range, min. | 219.52 | |||
| Temperature range, max. | 459.98 | |||
| λliquid | 0.14 | W/m×K | 219.52 | Calculated Property |
| λliquid | 0.13 | W/m×K | 246.24 | Calculated Property |
| λliquid | 0.13 | W/m×K | 272.96 | Calculated Property |
| λliquid | 0.12 | W/m×K | 299.67 | Calculated Property |
| λliquid | 0.12 | W/m×K | 326.39 | Calculated Property |
| λliquid | 0.11 | W/m×K | 353.11 | Calculated Property |
| λliquid | 0.11 | W/m×K | 379.83 | Calculated Property |
| λliquid | 0.10 | W/m×K | 406.54 | Calculated Property |
| λliquid | 0.10 | W/m×K | 433.26 | Calculated Property |
| λliquid | 0.09 | W/m×K | 459.98 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 2-ethyl-1,4-dimethyl-.
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).
- 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
- Crippen Method
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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