- InChI
- InChI=1S/C10H14/c1-3-9-7-5-6-8-10(9)4-2/h5-8H,3-4H2,1-2H3
- InChI Key
- KVNYFPKFSJIPBJ-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCc1ccccc1CC
- Molecular Weight1
- 134.22
- CAS
- 135-01-3
- Other Names
-
- 1,2-DiethyIbenzene
- 1,2-Diethylbenzene
- Benzene, o-diethyl-
- o-Diethylbenzene
- ortho-Diethylbenzene
- 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).
- 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).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- 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 | [0.3540; 0.3879] |
|
|
| ω | 0.3879 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3540 | KDB | |
| ΔcH°liquid | [-5867.43; -5865.10] | kJ/mol |
|
| ΔcH°liquid | -5867.43 ± 0.88 | kJ/mol | NIST |
| ΔcH°liquid | -5865.10 ± 1.80 | kJ/mol | NIST |
| μ | 0.59 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 141.08 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -18.95 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | [-70.90; -68.50] | kJ/mol |
|
| ΔfH°liquid | -68.50 ± 1.00 | kJ/mol | NIST |
| ΔfH°liquid | -70.90 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.80 | kJ/mol | NIST |
| IE | [8.51; 8.51] | eV |
|
| IE | 8.51 | eV | NIST |
| IE | 8.51 | eV | NIST |
| log10WS | [-3.28; -3.28] |
|
|
| log10WS | -3.28 | Aq. Solubility Prediction | |
| log10WS | -3.28 | Estimated Solubility | |
| logPoct/wat | 2.811 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 2 | KDB | |
| NFPA Health | 2 | KDB | |
| Pc | [2880.00; 2990.00] | kPa |
|
| Pc | 2880.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2990.00 | kPa | KDB |
| Ptriple | 1.04e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [1023.00; 1088.00] |
|
|
| Inp | 1041.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1051.80 | NIST | |
| Inp | 1057.90 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1043.50 | NIST | |
| Inp | 1064.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1066.00 | NIST | |
| Inp | 1034.80 | NIST | |
| Inp | 1038.10 | NIST | |
| Inp | 1052.70 | NIST | |
| Inp | 1058.90 | NIST | |
| Inp | 1065.90 | NIST | |
| Inp | 1042.70 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1034.80 | NIST | |
| Inp | 1038.10 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1042.70 | NIST | |
| Inp | 1039.10 | NIST | |
| Inp | 1043.60 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1067.00 | NIST | |
| Inp | 1051.70 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1049.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1056.70 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1043.30 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1059.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1048.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1068.80 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1057.00 | NIST | |
| Inp | Outlier 1088.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | Outlier 1023.00 | NIST | |
| Inp | 1044.00 | NIST | |
| Inp | 1052.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1051.50 | NIST | |
| Inp | 1058.70 | NIST | |
| Inp | 1055.80 | NIST | |
| Inp | 1057.20 | NIST | |
| Inp | 1039.30 | NIST | |
| Inp | 1043.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1042.00 | NIST | |
| Ip | [1285.00; 1379.00] |
|
|
| Ip | 1285.00 | NIST | |
| Ip | 1289.00 | NIST | |
| Ip | 1324.00 | NIST | |
| Ip | 1298.80 | NIST | |
| Ip | 1298.80 | NIST | |
| Ip | 1305.00 | NIST | |
| Ip | 1335.00 | NIST | |
| Ip | 1337.00 | NIST | |
| Ip | 1350.00 | NIST | |
| Ip | 1363.00 | NIST | |
| Ip | Outlier 1379.00 | NIST | |
| Ip | 1324.00 | NIST | |
| Ip | 1299.00 | NIST | |
| Ip | 1372.00 | NIST | |
| Ip | 1324.00 | NIST | |
| Ip | 1299.00 | NIST | |
| Ip | 1324.00 | NIST | |
| Ip | 1308.50 | NIST | |
| Tboil | [449.70; 457.40] | K |
|
| Tboil | 456.57 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 457.00 | K | KDB |
| Tboil | 456.70 | K | NIST |
| Tboil | 456.00 ± 2.00 | K | NIST |
| Tboil | 456.45 ± 0.20 | K | NIST |
| Tboil | 456.45 ± 0.20 | K | NIST |
| Tboil | 456.57 ± 0.03 | K | NIST |
| Tboil | 456.45 ± 0.30 | K | NIST |
| Tboil | 456.90 ± 2.00 | K | NIST |
| Tboil | Outlier 449.70 ± 1.00 | K | NIST |
| Tboil | 454.35 ± 0.30 | K | NIST |
| Tboil | 456.70 ± 0.50 | K | NIST |
| Tboil | 456.45 ± 0.30 | K | NIST |
| Tboil | 457.40 ± 1.00 | K | NIST |
| Tboil | 456.00 ± 2.00 | K | NIST |
| Tboil | Outlier 450.00 ± 7.00 | K | NIST |
| Tboil | 457.00 ± 2.00 | K | NIST |
| Tc | [668.00; 669.60] | K |
|
| Tc | 668.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 669.60 | K | KDB |
| Tfus | [241.71; 242.15] | K |
|
| Tfus | 242.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 241.91 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 242.00 | K | KDB |
| Tfus | 242.08 | K | Aq. Solubility Prediction |
| Tfus | 241.71 ± 0.20 | K | NIST |
| Ttriple | 241.93 | K | ChemSep v8.3 pure component data Compiled value |
| UQi | 4.62 | ChemSep v8.3 pure component data Compiled value | |
| URi | 6.01 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.487; 0.502] | m3/kmol |
|
| Vc | 0.502 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.487 | m3/kmol | KDB |
| Zc | [0.2600000; 0.2618150] |
|
|
| Zc | 0.2600000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2618150 | KDB | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.41; 46.00] | kJ/mol | [416.50; 457.00] |
|
| ΔvapH | 46.00 | kJ/mol | 416.50 | NIST |
| ΔvapH | 39.41 | kJ/mol | 457.00 | KDB |
| n0 | 1.50106 | 298.15 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [141.46; 476.56] | J/mol×K | [200.00; 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 | 1.22330e+02 | |||
| Coefficient B | -7.23390e+02 | |||
| Coefficient C | 6.62324e+00 | |||
| Coefficient D | -2.89530e-04 | |||
| Coefficient E | 7.25620e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 141.46 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 206.43 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 273.65 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 328.11 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 369.95 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 401.98 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 426.87 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 446.65 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 462.84 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 476.56 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [211.33; 320.85] | J/mol×K | [241.93; 456.61] |
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 | 1.37310e+01 | |||
| Coefficient B | 7.92270e+00 | |||
| Coefficient C | 4.32924e+00 | |||
| Coefficient D | 4.71800e-03 | |||
| Coefficient E | -3.71060e-06 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 456.61 | |||
| Cp,liquid | 211.33 | J/mol×K | 241.93 | Calculated Property |
| Cp,liquid | 224.53 | J/mol×K | 265.78 | Calculated Property |
| Cp,liquid | 237.77 | J/mol×K | 289.64 | Calculated Property |
| Cp,liquid | 250.93 | J/mol×K | 313.49 | Calculated Property |
| Cp,liquid | 263.88 | J/mol×K | 337.34 | Calculated Property |
| Cp,liquid | 276.48 | J/mol×K | 361.20 | Calculated Property |
| Cp,liquid | 288.61 | J/mol×K | 385.05 | Calculated Property |
| Cp,liquid | 300.14 | J/mol×K | 408.90 | Calculated Property |
| Cp,liquid | 310.92 | J/mol×K | 432.76 | Calculated Property |
| Cp,liquid | 320.85 | J/mol×K | 456.61 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0037987; 0.0001057] | Pa×s | [241.93; 550.00] |
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 | -1.39710e+01 | |||
| Coefficient B | 1.60870e+03 | |||
| Coefficient C | 3.23950e-01 | |||
| Coefficient D | -5.05330e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 550.00 | |||
| η | 0.0037987 | Pa×s | 241.93 | Calculated Property |
| η | 0.0017235 | Pa×s | 276.16 | Calculated Property |
| η | 0.0009321 | Pa×s | 310.39 | Calculated Property |
| η | 0.0005697 | Pa×s | 344.62 | Calculated Property |
| η | 0.0003805 | Pa×s | 378.85 | Calculated Property |
| η | 0.0002715 | Pa×s | 413.08 | Calculated Property |
| η | 0.0002038 | Pa×s | 447.31 | Calculated Property |
| η | 0.0001590 | Pa×s | 481.54 | Calculated Property |
| η | 0.0001280 | Pa×s | 515.77 | Calculated Property |
| η | 0.0001057 | Pa×s | 550.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [53.80; 15.98] | kJ/mol | [241.93; 645.58] |
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 | 4.48270e+01 | |||
| Coefficient B | -1.90730e+00 | |||
| Coefficient C | 6.12950e+00 | |||
| Coefficient D | -6.37720e+00 | |||
| Coefficient E | 2.48570e+00 | |||
| Critical temperature, Tc (K) | 6.68000e+02 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 645.58 | |||
| ΔvapH | 53.80 | kJ/mol | 241.93 | Calculated Property |
| ΔvapH | 51.71 | kJ/mol | 286.78 | Calculated Property |
| ΔvapH | 49.07 | kJ/mol | 331.63 | Calculated Property |
| ΔvapH | 46.09 | kJ/mol | 376.48 | Calculated Property |
| ΔvapH | 42.84 | kJ/mol | 421.33 | Calculated Property |
| ΔvapH | 39.33 | kJ/mol | 466.18 | Calculated Property |
| ΔvapH | 35.43 | kJ/mol | 511.03 | Calculated Property |
| ΔvapH | 30.83 | kJ/mol | 555.88 | Calculated Property |
| ΔvapH | 24.95 | kJ/mol | 600.73 | Calculated Property |
| ΔvapH | 15.98 | kJ/mol | 645.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [334.02; 487.32] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.42021e+01 | |||
| Coefficient B | -3.77470e+03 | |||
| Coefficient C | -6.27460e+01 | |||
| Temperature range, min. | 334.02 | |||
| Temperature range, max. | 487.32 | |||
| Pvap | 1.33 | kPa | 334.02 | Calculated Property |
| Pvap | 3.03 | kPa | 351.05 | Calculated Property |
| Pvap | 6.30 | kPa | 368.09 | Calculated Property |
| Pvap | 12.10 | kPa | 385.12 | Calculated Property |
| Pvap | 21.77 | kPa | 402.15 | Calculated Property |
| Pvap | 37.04 | kPa | 419.19 | Calculated Property |
| Pvap | 60.05 | kPa | 436.22 | Calculated Property |
| Pvap | 93.31 | kPa | 453.25 | Calculated Property |
| Pvap | 139.77 | kPa | 470.29 | Calculated Property |
| Pvap | 202.66 | kPa | 487.32 | Calculated Property |
| Pvap | [7.32e-04; 2880.00] | kPa | [241.93; 646.05] |
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 | 1.29277e+02 | |||
| Coefficient B | -1.07608e+04 | |||
| Coefficient C | -1.68823e+01 | |||
| Coefficient D | 1.09939e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 668 K. | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 646.05 | |||
| Pvap | 7.32e-04 | kPa | 241.93 | Calculated Property |
| Pvap | 0.06 | kPa | 286.83 | Calculated Property |
| Pvap | 1.06 | kPa | 331.73 | Calculated Property |
| Pvap | 8.43 | kPa | 376.64 | Calculated Property |
| Pvap | 39.15 | kPa | 421.54 | Calculated Property |
| Pvap | 128.31 | kPa | 466.44 | Calculated Property |
| Pvap | 334.06 | kPa | 511.34 | Calculated Property |
| Pvap | 747.05 | kPa | 556.25 | Calculated Property |
| Pvap | 1513.04 | kPa | 601.15 | Calculated Property |
| Pvap | 2880.00 | kPa | 646.05 | Calculated Property |
| Pvap | [1.03e-03; 2825.37] | kPa | [241.93; 668.00] |
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 | 7.81349e+01 | |||
| Coefficient B | -8.61176e+03 | |||
| Coefficient C | -9.03986e+00 | |||
| Coefficient D | 3.36428e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 668.00 | |||
| Pvap | 1.03e-03 | kPa | 241.93 | Calculated Property |
| Pvap | 0.08 | kPa | 289.27 | Calculated Property |
| Pvap | 1.39 | kPa | 336.61 | Calculated Property |
| Pvap | 11.13 | kPa | 383.95 | Calculated Property |
| Pvap | 51.96 | kPa | 431.29 | Calculated Property |
| Pvap | 168.83 | kPa | 478.64 | Calculated Property |
| Pvap | 426.53 | kPa | 525.98 | Calculated Property |
| Pvap | 901.13 | kPa | 573.32 | Calculated Property |
| Pvap | 1672.89 | kPa | 620.66 | Calculated Property |
| Pvap | 2825.37 | kPa | 668.00 | Calculated Property |
| Pvap | [6.42; 104.02] | kPa | [369.88; 457.64] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40804e+01 | |||
| Coefficient B | -3.63324e+03 | |||
| Coefficient C | -7.25960e+01 | |||
| Reference | Forziati, Norris, et al., 1949, 2 | |||
| Temperature range, min. | 369.88 | |||
| Temperature range, max. | 457.64 | |||
| Pvap | 6.42 | kPa | 369.88 | Calculated Property |
| Pvap | 9.46 | kPa | 379.63 | Calculated Property |
| Pvap | 13.62 | kPa | 389.38 | Calculated Property |
| Pvap | 19.18 | kPa | 399.13 | Calculated Property |
| Pvap | 26.48 | kPa | 408.88 | Calculated Property |
| Pvap | 35.91 | kPa | 418.64 | Calculated Property |
| Pvap | 47.88 | kPa | 428.39 | Calculated Property |
| Pvap | 62.87 | kPa | 438.14 | Calculated Property |
| Pvap | 81.40 | kPa | 447.89 | Calculated Property |
| Pvap | 104.02 | kPa | 457.64 | Calculated Property |
| Pvap | [6.42; 104.02] | kPa | [369.88; 457.64] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.40804e+01 | |||
| Coefficient B | -3.63324e+03 | |||
| Coefficient C | -7.25960e+01 | |||
| Reference | Forziati, Norris, et al., 1949 | |||
| Temperature range, min. | 369.88 | |||
| Temperature range, max. | 457.64 | |||
| Pvap | 6.42 | kPa | 369.88 | Calculated Property |
| Pvap | 9.46 | kPa | 379.63 | Calculated Property |
| Pvap | 13.62 | kPa | 389.38 | Calculated Property |
| Pvap | 19.18 | kPa | 399.13 | Calculated Property |
| Pvap | 26.48 | kPa | 408.88 | Calculated Property |
| Pvap | 35.91 | kPa | 418.64 | Calculated Property |
| Pvap | 47.88 | kPa | 428.39 | Calculated Property |
| Pvap | 62.87 | kPa | 438.14 | Calculated Property |
| Pvap | 81.40 | kPa | 447.89 | Calculated Property |
| Pvap | 104.02 | kPa | 457.64 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [918.83; 462.27] | kg/m3 | [241.93; 645.58] |
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 | 6.99089e+01 | |||
| Coefficient B | 2.53890e-01 | |||
| Coefficient C | 6.68000e+02 | |||
| Coefficient D | 2.86660e-01 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 645.58 | |||
| ρl | 918.83 | kg/m3 | 241.93 | Calculated Property |
| ρl | 884.74 | kg/m3 | 286.78 | Calculated Property |
| ρl | 849.08 | kg/m3 | 331.63 | Calculated Property |
| ρl | 811.50 | kg/m3 | 376.48 | Calculated Property |
| ρl | 771.51 | kg/m3 | 421.33 | Calculated Property |
| ρl | 728.33 | kg/m3 | 466.18 | Calculated Property |
| ρl | 680.71 | kg/m3 | 511.03 | Calculated Property |
| ρl | 626.35 | kg/m3 | 555.88 | Calculated Property |
| ρl | 560.01 | kg/m3 | 600.73 | Calculated Property |
| ρl | 462.27 | kg/m3 | 645.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 5.53e-04] | N/m | [241.93; 645.58] |
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 | -9.38070e-02 | |||
| Coefficient B | -2.72320e+01 | |||
| Coefficient C | -1.59350e+00 | |||
| Coefficient D | -1.56450e-03 | |||
| Coefficient E | 6.83950e-07 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 645.58 | |||
| γ | 0.04 | N/m | 241.93 | Calculated Property |
| γ | 0.03 | N/m | 286.78 | Calculated Property |
| γ | 0.03 | N/m | 331.63 | Calculated Property |
| γ | 0.02 | N/m | 376.48 | Calculated Property |
| γ | 0.02 | N/m | 421.33 | Calculated Property |
| γ | 0.01 | N/m | 466.18 | Calculated Property |
| γ | 0.01 | N/m | 511.03 | Calculated Property |
| γ | 0.01 | N/m | 555.88 | Calculated Property |
| γ | 0.00 | N/m | 600.73 | Calculated Property |
| γ | 5.53e-04 | N/m | 645.58 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.01; 0.07] | W/m×K | [241.93; 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 | 8.78510e-05 | |||
| Coefficient B | 1.03970e+00 | |||
| Coefficient C | 5.05400e+02 | |||
| Coefficient D | 4.74660e+04 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.01 | W/m×K | 241.93 | Calculated Property |
| λgas | 0.01 | W/m×K | 326.16 | Calculated Property |
| λgas | 0.02 | W/m×K | 410.39 | Calculated Property |
| λgas | 0.03 | W/m×K | 494.62 | Calculated Property |
| λgas | 0.03 | W/m×K | 578.85 | Calculated Property |
| λgas | 0.04 | W/m×K | 663.08 | Calculated Property |
| λgas | 0.05 | W/m×K | 747.31 | Calculated Property |
| λgas | 0.06 | W/m×K | 831.54 | Calculated Property |
| λgas | 0.07 | W/m×K | 915.77 | 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 | [241.93; 456.61] |
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 | -4.72180e-02 | |||
| Coefficient B | -1.10730e+01 | |||
| Coefficient C | -1.41890e+00 | |||
| Coefficient D | -7.77870e-04 | |||
| Coefficient E | -7.52520e-07 | |||
| Temperature range, min. | 241.93 | |||
| Temperature range, max. | 456.61 | |||
| λliquid | 0.14 | W/m×K | 241.93 | Calculated Property |
| λliquid | 0.13 | W/m×K | 265.78 | Calculated Property |
| λliquid | 0.13 | W/m×K | 289.64 | Calculated Property |
| λliquid | 0.12 | W/m×K | 313.49 | Calculated Property |
| λliquid | 0.12 | W/m×K | 337.34 | Calculated Property |
| λliquid | 0.11 | W/m×K | 361.20 | Calculated Property |
| λliquid | 0.11 | W/m×K | 385.05 | Calculated Property |
| λliquid | 0.10 | W/m×K | 408.90 | Calculated Property |
| λliquid | 0.10 | W/m×K | 432.76 | Calculated Property |
| λliquid | 0.09 | W/m×K | 456.61 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,2-diethyl-.
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).
- 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
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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