- InChI
- InChI=1S/C10H14/c1-4-10-6-5-8(2)7-9(10)3/h5-7H,4H2,1-3H3
- InChI Key
- MEMBJMDZWKVOTB-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCc1ccc(C)cc1C
- Molecular Weight1
- 134.22
- CAS
- 874-41-9
- Other Names
-
- 1,3-Dimethyl-4-ethylbenzene
- 1-Ethyl-2,4-dimethylbenzene
- 2,4-Dimethyl-1-ethylbenzene
- 4-Ethyl m-xylene
- 4-Ethyl-1,3-dimethylbenzene
- 4-Ethyl-m-xylene
- m-Xylene, 4-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 | [0.4090; 0.4331] |
|
|
| ω | 0.4331 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.4090 | ChemSep v8.3 pure component data Compiled value | |
| ΔcH°liquid | -5851.80 ± 1.10 | kJ/mol | NIST |
| ΔfG° | 128.60 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -30.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | -84.10 ± 1.30 | kJ/mol | NIST |
| ΔfusH° | 14.92 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 53.30 | kJ/mol | NIST |
| IE | 8.20 | eV | Relay (1.0) Calculated Property |
| log10WS | -3.81 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.866 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| Pc | [2850.00; 2899.92] | kPa |
|
| Pc | 2899.92 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2850.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Ptriple | 1.81e-05 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1034.00; 1097.00] |
|
|
| Inp | 1070.80 | NIST | |
| Inp | 1074.20 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1068.70 | NIST | |
| Inp | 1069.60 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | Outlier 1096.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1061.70 | NIST | |
| Inp | 1061.80 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1060.40 | NIST | |
| Inp | 1085.00 | NIST | |
| Inp | 1089.00 | NIST | |
| Inp | Outlier 1093.00 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1080.00 | NIST | |
| Inp | 1060.50 | NIST | |
| Inp | 1066.60 | NIST | |
| Inp | 1070.80 | NIST | |
| Inp | 1077.80 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | Outlier 1097.00 | NIST | |
| Inp | 1069.60 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1070.80 | NIST | |
| Inp | 1086.60 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1063.94 | NIST | |
| Inp | 1064.79 | NIST | |
| Inp | 1065.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1076.67 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1068.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1073.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1083.50 | NIST | |
| Inp | 1061.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Inp | Outlier 1034.00 | NIST | |
| Inp | 1078.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1062.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1069.00 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1071.00 | NIST | |
| Inp | 1075.00 | NIST | |
| Ip | [1316.00; 1373.00] |
|
|
| Ip | 1316.00 | NIST | |
| Ip | 1350.00 | NIST | |
| Ip | 1342.80 | NIST | |
| Ip | 1347.00 | NIST | |
| Ip | Outlier 1373.00 | NIST | |
| Ip | 1326.00 | NIST | |
| Ip | 1348.00 | NIST | |
| Ip | 1348.00 | NIST | |
| Ip | 1350.00 | NIST | |
| Ip | 1330.00 | NIST | |
| Ip | 1346.00 | NIST | |
| Ip | 1316.00 | NIST | |
| Ip | 1348.00 | NIST | |
| Tboil | [461.35; 464.20] | K |
|
| Tboil | 461.59 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 461.40 | K | NIST |
| Tboil | 461.35 ± 0.10 | K | NIST |
| Tboil | 461.37 ± 0.20 | K | NIST |
| Tboil | 461.48 ± 0.30 | K | NIST |
| Tboil | 461.60 ± 0.30 | K | NIST |
| Tboil | 461.56 ± 0.30 | K | NIST |
| Tboil | 461.40 ± 1.00 | K | NIST |
| Tboil | 461.60 ± 0.15 | K | NIST |
| Tboil | Outlier 464.20 ± 2.00 | K | NIST |
| Tboil | 461.60 ± 0.30 | K | NIST |
| Tboil | 461.56 ± 0.20 | K | NIST |
| Tboil | 461.60 ± 0.30 | K | NIST |
| Tc | [662.60; 665.00] | K |
|
| Tc | 662.60 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 665.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | [210.00; 210.27] | K |
|
| Tfus | 210.20 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 210.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 210.27 ± 0.02 | K | NIST |
| Tfus | 210.14 ± 0.20 | K | NIST |
| Ttriple | 210.27 | 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 | [0.456; 0.482] | m3/kmol |
|
| Vc | 0.482 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.456 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Zc | 0.2510000 | ChemSep v8.3 pure component data Compiled value | |
| Zra | 0.25 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 48.50 | kJ/mol | 415.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [178.88; 474.81] | J/mol×K | [298.15; 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. | 298.15 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 178.88 | J/mol×K | 298.15 | Calculated Property |
| Cp,gas | 246.04 | J/mol×K | 431.69 | Calculated Property |
| Cp,gas | 300.94 | J/mol×K | 565.23 | Calculated Property |
| Cp,gas | 344.66 | J/mol×K | 698.77 | Calculated Property |
| Cp,gas | 379.59 | J/mol×K | 832.31 | Calculated Property |
| Cp,gas | 407.70 | J/mol×K | 965.84 | Calculated Property |
| Cp,gas | 430.41 | J/mol×K | 1099.38 | Calculated Property |
| Cp,gas | 448.71 | J/mol×K | 1232.92 | Calculated Property |
| Cp,gas | 463.33 | J/mol×K | 1366.46 | Calculated Property |
| Cp,gas | 474.81 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [247.89; 326.29] | J/mol×K | [298.15; 461.59] |
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 | 9.56990e+01 | |||
| Coefficient B | -8.44310e+01 | |||
| Coefficient C | 4.15824e+00 | |||
| Coefficient D | 5.10320e-03 | |||
| Coefficient E | -4.17850e-06 | |||
| Temperature range, min. | 298.15 | |||
| Temperature range, max. | 461.59 | |||
| Cp,liquid | 247.89 | J/mol×K | 298.15 | Calculated Property |
| Cp,liquid | 257.67 | J/mol×K | 316.31 | Calculated Property |
| Cp,liquid | 267.31 | J/mol×K | 334.47 | Calculated Property |
| Cp,liquid | 276.75 | J/mol×K | 352.63 | Calculated Property |
| Cp,liquid | 285.94 | J/mol×K | 370.79 | Calculated Property |
| Cp,liquid | 294.82 | J/mol×K | 388.95 | Calculated Property |
| Cp,liquid | 303.35 | J/mol×K | 407.11 | Calculated Property |
| Cp,liquid | 311.48 | J/mol×K | 425.27 | Calculated Property |
| Cp,liquid | 319.14 | J/mol×K | 443.43 | Calculated Property |
| Cp,liquid | 326.29 | J/mol×K | 461.59 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0070992; 0.0001078] | Pa×s | [210.27; 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 | -1.26650e+01 | |||
| Coefficient B | 1.41950e+03 | |||
| Coefficient C | 1.83540e-01 | |||
| Coefficient D | -3.45100e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 573.00 | |||
| η | 0.0070992 | Pa×s | 210.27 | Calculated Property |
| η | 0.0024594 | Pa×s | 250.57 | Calculated Property |
| η | 0.0011443 | Pa×s | 290.88 | Calculated Property |
| η | 0.0006415 | Pa×s | 331.18 | Calculated Property |
| η | 0.0004075 | Pa×s | 371.48 | Calculated Property |
| η | 0.0002826 | Pa×s | 411.79 | Calculated Property |
| η | 0.0002089 | Pa×s | 452.09 | Calculated Property |
| η | 0.0001620 | Pa×s | 492.39 | Calculated Property |
| η | 0.0001303 | Pa×s | 532.70 | Calculated Property |
| η | 0.0001078 | Pa×s | 573.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [53.68; 18.45] | kJ/mol | [210.27; 641.07] |
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 | 6.58648e+01 | |||
| Coefficient B | 9.58711e-01 | |||
| Coefficient C | -1.95219e+00 | |||
| Coefficient D | 2.24001e+00 | |||
| Coefficient E | -8.65941e-01 | |||
| Critical temperature, Tc (K) | 6.65000e+02 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 641.07 | |||
| ΔvapH | 53.68 | kJ/mol | 210.27 | Calculated Property |
| ΔvapH | 51.83 | kJ/mol | 258.14 | Calculated Property |
| ΔvapH | 49.90 | kJ/mol | 306.00 | Calculated Property |
| ΔvapH | 47.74 | kJ/mol | 353.87 | Calculated Property |
| ΔvapH | 45.22 | kJ/mol | 401.74 | Calculated Property |
| ΔvapH | 42.19 | kJ/mol | 449.60 | Calculated Property |
| ΔvapH | 38.51 | kJ/mol | 497.47 | Calculated Property |
| ΔvapH | 33.94 | kJ/mol | 545.34 | Calculated Property |
| ΔvapH | 27.95 | kJ/mol | 593.20 | Calculated Property |
| ΔvapH | 18.45 | kJ/mol | 641.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.65] | kPa | [337.49; 491.95] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48165e+01 | |||
| Coefficient B | -4.24584e+03 | |||
| Coefficient C | -4.52570e+01 | |||
| Temperature range, min. | 337.49 | |||
| Temperature range, max. | 491.95 | |||
| Pvap | 1.33 | kPa | 337.49 | Calculated Property |
| Pvap | 2.98 | kPa | 354.65 | Calculated Property |
| Pvap | 6.14 | kPa | 371.81 | Calculated Property |
| Pvap | 11.75 | kPa | 388.98 | Calculated Property |
| Pvap | 21.14 | kPa | 406.14 | Calculated Property |
| Pvap | 36.07 | kPa | 423.30 | Calculated Property |
| Pvap | 58.74 | kPa | 440.46 | Calculated Property |
| Pvap | 91.86 | kPa | 457.63 | Calculated Property |
| Pvap | 138.61 | kPa | 474.79 | Calculated Property |
| Pvap | 202.65 | kPa | 491.95 | Calculated Property |
| Pvap | [6.43e-06; 2835.95] | kPa | [210.27; 665.00] |
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 | 1.02692e+02 | |||
| Coefficient B | -9.84970e+03 | |||
| Coefficient C | -1.27300e+01 | |||
| Coefficient D | 6.35820e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 665.00 | |||
| Pvap | 6.43e-06 | kPa | 210.27 | Calculated Property |
| Pvap | 4.21e-03 | kPa | 260.80 | Calculated Property |
| Pvap | 0.24 | kPa | 311.32 | Calculated Property |
| Pvap | 3.70 | kPa | 361.85 | Calculated Property |
| Pvap | 25.25 | kPa | 412.37 | Calculated Property |
| Pvap | 104.15 | kPa | 462.90 | Calculated Property |
| Pvap | 309.42 | kPa | 513.42 | Calculated Property |
| Pvap | 738.57 | kPa | 563.95 | Calculated Property |
| Pvap | 1521.01 | kPa | 614.47 | Calculated Property |
| Pvap | 2835.95 | kPa | 665.00 | Calculated Property |
| Pvap | [1.79e-05; 2797.80] | kPa | [210.27; 665.00] |
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 | 5.98927e+01 | |||
| Coefficient B | -7.79291e+03 | |||
| Coefficient C | -6.32939e+00 | |||
| Coefficient D | 2.04034e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 665.00 | |||
| Pvap | 1.79e-05 | kPa | 210.27 | Calculated Property |
| Pvap | 6.31e-03 | kPa | 260.80 | Calculated Property |
| Pvap | 0.28 | kPa | 311.32 | Calculated Property |
| Pvap | 3.80 | kPa | 361.85 | Calculated Property |
| Pvap | 25.20 | kPa | 412.37 | Calculated Property |
| Pvap | 104.39 | kPa | 462.90 | Calculated Property |
| Pvap | 314.13 | kPa | 513.42 | Calculated Property |
| Pvap | 754.93 | kPa | 563.95 | Calculated Property |
| Pvap | 1542.66 | kPa | 614.47 | Calculated Property |
| Pvap | 2797.80 | kPa | 665.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [940.05; 463.66] | kg/m3 | [210.27; 641.07] |
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 | 7.13826e+01 | |||
| Coefficient B | 2.56350e-01 | |||
| Coefficient C | 6.65000e+02 | |||
| Coefficient D | 2.95350e-01 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 641.07 | |||
| ρl | 940.05 | kg/m3 | 210.27 | Calculated Property |
| ρl | 903.81 | kg/m3 | 258.14 | Calculated Property |
| ρl | 866.00 | kg/m3 | 306.00 | Calculated Property |
| ρl | 826.28 | kg/m3 | 353.87 | Calculated Property |
| ρl | 784.13 | kg/m3 | 401.74 | Calculated Property |
| ρl | 738.77 | kg/m3 | 449.60 | Calculated Property |
| ρl | 688.96 | kg/m3 | 497.47 | Calculated Property |
| ρl | 632.38 | kg/m3 | 545.34 | Calculated Property |
| ρl | 563.75 | kg/m3 | 593.20 | Calculated Property |
| ρl | 463.66 | kg/m3 | 641.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 7.92e-04] | N/m | [210.27; 641.07] |
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 | -1.53470e-02 | |||
| Coefficient B | 6.63400e+01 | |||
| Coefficient C | -3.09100e+00 | |||
| Coefficient D | 3.18640e-04 | |||
| Coefficient E | -3.26860e-06 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 641.07 | |||
| γ | 0.04 | N/m | 210.27 | Calculated Property |
| γ | 0.04 | N/m | 258.14 | Calculated Property |
| γ | 0.03 | N/m | 306.00 | Calculated Property |
| γ | 0.03 | N/m | 353.87 | Calculated Property |
| γ | 0.02 | N/m | 401.74 | Calculated Property |
| γ | 0.02 | N/m | 449.60 | Calculated Property |
| γ | 0.01 | N/m | 497.47 | Calculated Property |
| γ | 0.01 | N/m | 545.34 | Calculated Property |
| γ | 0.00 | N/m | 593.20 | Calculated Property |
| γ | 7.92e-04 | N/m | 641.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [210.27; 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 | 8.35470e-05 | |||
| Coefficient B | 1.04820e+00 | |||
| Coefficient C | 5.20640e+02 | |||
| Coefficient D | 4.51000e+04 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 210.27 | Calculated Property |
| λgas | 0.01 | W/m×K | 298.02 | Calculated Property |
| λgas | 0.02 | W/m×K | 385.77 | Calculated Property |
| λgas | 0.02 | W/m×K | 473.51 | Calculated Property |
| λgas | 0.03 | W/m×K | 561.26 | Calculated Property |
| λgas | 0.04 | W/m×K | 649.01 | Calculated Property |
| λgas | 0.05 | W/m×K | 736.76 | Calculated Property |
| λgas | 0.06 | W/m×K | 824.50 | Calculated Property |
| λgas | 0.07 | W/m×K | 912.25 | 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 | [210.27; 461.59] |
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 | -8.11710e-02 | |||
| Coefficient B | 5.05870e+00 | |||
| Coefficient C | -1.41950e+00 | |||
| Coefficient D | -3.17480e-04 | |||
| Coefficient E | -9.17560e-07 | |||
| Temperature range, min. | 210.27 | |||
| Temperature range, max. | 461.59 | |||
| λliquid | 0.14 | W/m×K | 210.27 | Calculated Property |
| λliquid | 0.14 | W/m×K | 238.19 | Calculated Property |
| λliquid | 0.13 | W/m×K | 266.12 | Calculated Property |
| λliquid | 0.13 | W/m×K | 294.04 | Calculated Property |
| λliquid | 0.12 | W/m×K | 321.97 | Calculated Property |
| λliquid | 0.12 | W/m×K | 349.89 | Calculated Property |
| λliquid | 0.11 | W/m×K | 377.82 | Calculated Property |
| λliquid | 0.10 | W/m×K | 405.74 | Calculated Property |
| λliquid | 0.10 | W/m×K | 433.67 | Calculated Property |
| λliquid | 0.09 | W/m×K | 461.59 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1-ethyl-2,4-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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