- InChI
- InChI=1S/C10H14/c1-3-9-6-5-7-10(4-2)8-9/h5-8H,3-4H2,1-2H3
- InChI Key
- AFZZYIJIWUTJFO-UHFFFAOYSA-N
- Formula
- C10H14
- SMILES
- CCc1cccc(CC)c1
- Molecular Weight1
- 134.22
- CAS
- 141-93-5
- Other Names
-
- 1,3-Diethylbenzene
- Benzene, m-diethyl-
- m-Diethylbenzene
- meta-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).
- 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; 0.3927] |
|
|
| ω | 0.3927 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3540 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3590 | KDB | |
| ΔcH°liquid | [-5863.00; -5862.41] | kJ/mol |
|
| ΔcH°liquid | -5862.41 ± 0.92 | kJ/mol | NIST |
| ΔcH°liquid | -5863.00 ± 1.80 | kJ/mol | NIST |
| μ | 0.36 | debye | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | 136.70 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -21.80 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°liquid | [-73.50; -73.00] | kJ/mol |
|
| ΔfH°liquid | -73.50 ± 1.10 | kJ/mol | NIST |
| ΔfH°liquid | -73.00 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 15.31 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 52.50 | kJ/mol | NIST |
| IE | [8.49; 8.49] | eV |
|
| IE | 8.49 | eV | NIST |
| IE | 8.49 ± 0.01 | eV | NIST |
| log10WS | -3.67 | Relay (1.0) Calculated Property | |
| logPoct/wat | 2.811 | Crippen Calculated Property | |
| McVol | 128.000 | ml/mol | McGowan Calculated Property |
| Pc | [2880.00; 2930.00] | kPa |
|
| Pc | 2919.17 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2880.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 2930.00 | kPa | KDB |
| Ptriple | 6.65e-07 | kPa | ChemSep v8.3 pure component data Compiled value |
| Inp | [186.60; 1070.00] |
|
|
| Inp | 1056.00 | NIST | |
| Inp | 1034.43 | NIST | |
| Inp | 1030.00 | NIST | |
| Inp | 1038.50 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1041.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1034.80 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1025.70 | NIST | |
| Inp | 1028.10 | NIST | |
| Inp | 1040.40 | NIST | |
| Inp | 1045.30 | NIST | |
| Inp | 1050.70 | NIST | |
| Inp | 1031.50 | NIST | |
| Inp | 1023.20 | NIST | |
| Inp | 1025.70 | NIST | |
| Inp | 1028.10 | NIST | |
| Inp | 1027.00 | NIST | |
| Inp | 1023.18 | NIST | |
| Inp | 1032.95 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1053.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1032.30 | NIST | |
| Inp | 1031.50 | NIST | |
| Inp | 1028.90 | NIST | |
| Inp | 1025.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1055.00 | NIST | |
| Inp | 1039.90 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1056.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1055.20 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1034.10 | NIST | |
| Inp | 1034.43 | NIST | |
| Inp | 1034.64 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1049.74 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1051.00 | NIST | |
| Inp | 1038.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1045.00 | NIST | |
| Inp | 1020.00 | NIST | |
| Inp | 1031.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1046.00 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1047.00 | NIST | |
| Inp | 1050.00 | NIST | |
| Inp | 1063.00 | NIST | |
| Inp | 1037.00 | NIST | |
| Inp | 1056.30 | NIST | |
| Inp | 1042.00 | NIST | |
| Inp | 1032.00 | NIST | |
| Inp | 1036.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1070.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1029.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1035.00 | NIST | |
| Inp | 1040.00 | NIST | |
| Inp | 1038.50 | NIST | |
| Inp | 1039.00 | NIST | |
| Inp | 1028.80 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1034.00 | NIST | |
| Inp | Outlier 186.60 | NIST | |
| Inp | 1033.00 | NIST | |
| Inp | 1039.90 | NIST | |
| Inp | 1049.74 | NIST | |
| Ip | [1275.80; 1348.00] |
|
|
| Ip | 1297.30 | NIST | |
| Ip | 1275.80 | NIST | |
| Ip | 1289.40 | NIST | |
| Ip | 1275.80 | NIST | |
| Ip | 1301.00 | NIST | |
| Ip | 1310.00 | NIST | |
| Ip | 1296.00 | NIST | |
| Ip | 1314.00 | NIST | |
| Ip | 1296.00 | NIST | |
| Ip | 1302.00 | NIST | |
| Ip | 1308.00 | NIST | |
| Ip | 1309.00 | NIST | |
| Ip | 1320.00 | NIST | |
| Ip | 1332.00 | NIST | |
| Ip | Outlier 1348.00 | NIST | |
| Ip | 1298.00 | NIST | |
| Ip | 1276.00 | NIST | |
| Ip | 1339.00 | NIST | |
| Ip | 1297.00 | NIST | |
| Ip | 1276.00 | NIST | |
| Ip | 1297.00 | NIST | |
| Ip | 1282.00 | NIST | |
| Ip | 1301.00 | NIST | |
| Ip | 1302.00 | NIST | |
| Tboil | [452.00; 456.00] | K |
|
| Tboil | 454.25 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 454.30 | K | KDB |
| Tboil | 454.30 | K | NIST |
| Tboil | 455.00 ± 2.00 | K | NIST |
| Tboil | Outlier 456.00 ± 2.00 | K | NIST |
| Tboil | 454.60 ± 0.30 | K | NIST |
| Tboil | 454.22 ± 0.30 | K | NIST |
| Tboil | 455.00 ± 2.00 | K | NIST |
| Tboil | 454.00 ± 2.00 | K | NIST |
| Tboil | 454.40 ± 0.20 | K | NIST |
| Tboil | 454.05 ± 1.00 | K | NIST |
| Tboil | 454.21 ± 0.30 | K | NIST |
| Tboil | 452.80 ± 2.00 | K | NIST |
| Tboil | 454.21 ± 0.20 | K | NIST |
| Tboil | 454.25 ± 0.20 | K | NIST |
| Tboil | 454.25 ± 0.20 | K | NIST |
| Tboil | 452.80 ± 3.00 | K | NIST |
| Tboil | 454.40 ± 0.40 | K | NIST |
| Tboil | 454.77 ± 0.20 | K | NIST |
| Tboil | 454.29 ± 0.20 | K | NIST |
| Tboil | 454.40 ± 0.20 | K | NIST |
| Tboil | 454.40 ± 0.20 | K | NIST |
| Tboil | 454.25 ± 0.50 | K | NIST |
| Tboil | Outlier 452.00 ± 3.00 | K | NIST |
| Tboil | 455.00 ± 1.00 | K | NIST |
| Tboil | 453.70 ± 0.50 | K | NIST |
| Tc | [657.10; 663.60] | K |
|
| Tc | 657.10 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 663.00 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 663.60 | K | KDB |
| Tfus | [189.00; 189.33] | K |
|
| Tfus | 189.20 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 189.23 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 189.00 | K | KDB |
| Tfus | 189.33 ± 0.20 | K | NIST |
| Tfus | 189.16 ± 0.20 | K | NIST |
| Tfus | 189.06 ± 0.15 | K | NIST |
| Ttriple | 189.26 | 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 | [0.468; 0.488] | m3/kmol |
|
| Vc | 0.468 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.488 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.487 | m3/kmol | KDB |
| Zc | [0.2550000; 0.2588800] |
|
|
| Zc | 0.2550000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2588800 | KDB | |
| Zra | 0.26 | ChemSep v8.3 pure component data Compiled value |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [39.37; 45.80] | kJ/mol | [412.50; 454.30] |
|
| ΔvapH | 45.80 | kJ/mol | 412.50 | NIST |
| ΔvapH | 39.37 | kJ/mol | 454.30 | KDB |
| n0 | 1.49310 | 298.15 | KDB |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [134.85; 476.69] | 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 | 1.15660e+02 | |||
| Coefficient B | -7.34220e+02 | |||
| Coefficient C | 6.69024e+00 | |||
| Coefficient D | -3.41860e-04 | |||
| Coefficient E | 8.93260e-08 | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 134.85 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 201.41 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 270.54 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 326.32 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 368.91 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 401.32 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 426.38 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 446.29 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 462.66 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 476.69 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [179.60; 317.23] | J/mol×K | [189.26; 454.29] |
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 | -1.50190e+01 | |||
| Coefficient B | 2.00980e+01 | |||
| Coefficient C | 4.44224e+00 | |||
| Coefficient D | 4.47040e-03 | |||
| Coefficient E | -3.44730e-06 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 454.29 | |||
| Cp,liquid | 179.60 | J/mol×K | 189.26 | Calculated Property |
| Cp,liquid | 194.95 | J/mol×K | 218.71 | Calculated Property |
| Cp,liquid | 210.93 | J/mol×K | 248.16 | Calculated Property |
| Cp,liquid | 227.23 | J/mol×K | 277.60 | Calculated Property |
| Cp,liquid | 243.59 | J/mol×K | 307.05 | Calculated Property |
| Cp,liquid | 259.75 | J/mol×K | 336.50 | Calculated Property |
| Cp,liquid | 275.43 | J/mol×K | 365.95 | Calculated Property |
| Cp,liquid | 290.41 | J/mol×K | 395.39 | Calculated Property |
| Cp,liquid | 304.42 | J/mol×K | 424.84 | Calculated Property |
| Cp,liquid | 317.23 | J/mol×K | 454.29 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0123897; 0.0001320] | Pa×s | [189.26; 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 | -1.15040e+01 | |||
| Coefficient B | 1.31360e+03 | |||
| Coefficient C | 3.35300e-02 | |||
| Coefficient D | -9.50740e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 550.00 | |||
| η | 0.0123897 | Pa×s | 189.26 | Calculated Property |
| η | 0.0037013 | Pa×s | 229.34 | Calculated Property |
| η | 0.0015842 | Pa×s | 269.42 | Calculated Property |
| η | 0.0008446 | Pa×s | 309.51 | Calculated Property |
| η | 0.0005200 | Pa×s | 349.59 | Calculated Property |
| η | 0.0003536 | Pa×s | 389.67 | Calculated Property |
| η | 0.0002582 | Pa×s | 429.75 | Calculated Property |
| η | 0.0001989 | Pa×s | 469.84 | Calculated Property |
| η | 0.0001595 | Pa×s | 509.92 | Calculated Property |
| η | 0.0001320 | Pa×s | 550.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [55.96; 17.24] | kJ/mol | [189.26; 638.07] |
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 | 6.46080e+01 | |||
| Coefficient B | 4.33681e-01 | |||
| Coefficient C | -2.44308e-02 | |||
| Coefficient D | 1.54888e-02 | |||
| Coefficient E | -2.45419e-02 | |||
| Critical temperature, Tc (K) | 6.63000e+02 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 638.07 | |||
| ΔvapH | 55.96 | kJ/mol | 189.26 | Calculated Property |
| ΔvapH | 53.40 | kJ/mol | 239.13 | Calculated Property |
| ΔvapH | 50.68 | kJ/mol | 289.00 | Calculated Property |
| ΔvapH | 47.77 | kJ/mol | 338.86 | Calculated Property |
| ΔvapH | 44.61 | kJ/mol | 388.73 | Calculated Property |
| ΔvapH | 41.12 | kJ/mol | 438.60 | Calculated Property |
| ΔvapH | 37.17 | kJ/mol | 488.47 | Calculated Property |
| ΔvapH | 32.51 | kJ/mol | 538.33 | Calculated Property |
| ΔvapH | 26.58 | kJ/mol | 588.20 | Calculated Property |
| ΔvapH | 17.24 | kJ/mol | 638.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [331.56; 484.84] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43625e+01 | |||
| Coefficient B | -3.88665e+03 | |||
| Coefficient C | -5.54190e+01 | |||
| Temperature range, min. | 331.56 | |||
| Temperature range, max. | 484.84 | |||
| Pvap | 1.33 | kPa | 331.56 | Calculated Property |
| Pvap | 3.02 | kPa | 348.59 | Calculated Property |
| Pvap | 6.25 | kPa | 365.62 | Calculated Property |
| Pvap | 12.00 | kPa | 382.65 | Calculated Property |
| Pvap | 21.60 | kPa | 399.68 | Calculated Property |
| Pvap | 36.78 | kPa | 416.72 | Calculated Property |
| Pvap | 59.69 | kPa | 433.75 | Calculated Property |
| Pvap | 92.92 | kPa | 450.78 | Calculated Property |
| Pvap | 139.46 | kPa | 467.81 | Calculated Property |
| Pvap | 202.67 | kPa | 484.84 | Calculated Property |
| Pvap | [2.72e-07; 2880.00] | kPa | [189.26; 618.93] |
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 | 1.46647e+02 | |||
| Coefficient B | -1.10909e+04 | |||
| Coefficient C | -1.97909e+01 | |||
| Coefficient D | 1.68460e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | Range stopped where the equation exceeds Pc; ChemSep gives it to 663 K. | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 618.93 | |||
| Pvap | 2.72e-07 | kPa | 189.26 | Calculated Property |
| Pvap | 5.99e-04 | kPa | 237.00 | Calculated Property |
| Pvap | 0.06 | kPa | 284.74 | Calculated Property |
| Pvap | 1.26 | kPa | 332.48 | Calculated Property |
| Pvap | 10.39 | kPa | 380.23 | Calculated Property |
| Pvap | 49.58 | kPa | 427.97 | Calculated Property |
| Pvap | 170.40 | kPa | 475.71 | Calculated Property |
| Pvap | 480.78 | kPa | 523.45 | Calculated Property |
| Pvap | 1211.13 | kPa | 571.19 | Calculated Property |
| Pvap | 2880.00 | kPa | 618.93 | Calculated Property |
| Pvap | [4.22e-07; 2884.55] | kPa | [189.26; 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 | 8.37996e+01 | |||
| Coefficient B | -8.84380e+03 | |||
| Coefficient C | -9.89795e+00 | |||
| Coefficient D | 4.12081e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 663.00 | |||
| Pvap | 4.22e-07 | kPa | 189.26 | Calculated Property |
| Pvap | 1.07e-03 | kPa | 241.90 | Calculated Property |
| Pvap | 0.12 | kPa | 294.54 | Calculated Property |
| Pvap | 2.51 | kPa | 347.17 | Calculated Property |
| Pvap | 20.90 | kPa | 399.81 | Calculated Property |
| Pvap | 96.92 | kPa | 452.45 | Calculated Property |
| Pvap | 307.75 | kPa | 505.09 | Calculated Property |
| Pvap | 758.34 | kPa | 557.72 | Calculated Property |
| Pvap | 1570.80 | kPa | 610.36 | Calculated Property |
| Pvap | 2884.55 | kPa | 663.00 | Calculated Property |
| Pvap | [6.42; 104.02] | kPa | [368.24; 455.31] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41169e+01 | |||
| Coefficient B | -3.62948e+03 | |||
| Coefficient C | -7.21460e+01 | |||
| Reference | Forziati, Norris, et al., 1949, 2 | |||
| Temperature range, min. | 368.24 | |||
| Temperature range, max. | 455.31 | |||
| Pvap | 6.42 | kPa | 368.24 | Calculated Property |
| Pvap | 9.46 | kPa | 377.91 | Calculated Property |
| Pvap | 13.61 | kPa | 387.59 | Calculated Property |
| Pvap | 19.17 | kPa | 397.26 | Calculated Property |
| Pvap | 26.47 | kPa | 406.94 | Calculated Property |
| Pvap | 35.89 | kPa | 416.61 | Calculated Property |
| Pvap | 47.86 | kPa | 426.29 | Calculated Property |
| Pvap | 62.85 | kPa | 435.96 | Calculated Property |
| Pvap | 81.39 | kPa | 445.64 | Calculated Property |
| Pvap | 104.02 | kPa | 455.31 | Calculated Property |
| Pvap | [6.42; 104.02] | kPa | [368.24; 455.31] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41169e+01 | |||
| Coefficient B | -3.62948e+03 | |||
| Coefficient C | -7.21460e+01 | |||
| Reference | Forziati, Norris, et al., 1949 | |||
| Temperature range, min. | 368.24 | |||
| Temperature range, max. | 455.31 | |||
| Pvap | 6.42 | kPa | 368.24 | Calculated Property |
| Pvap | 9.46 | kPa | 377.91 | Calculated Property |
| Pvap | 13.61 | kPa | 387.59 | Calculated Property |
| Pvap | 19.17 | kPa | 397.26 | Calculated Property |
| Pvap | 26.47 | kPa | 406.94 | Calculated Property |
| Pvap | 35.89 | kPa | 416.61 | Calculated Property |
| Pvap | 47.86 | kPa | 426.29 | Calculated Property |
| Pvap | 62.85 | kPa | 435.96 | Calculated Property |
| Pvap | 81.39 | kPa | 445.64 | Calculated Property |
| Pvap | 104.02 | kPa | 455.31 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [942.22; 460.63] | kg/m3 | [189.26; 638.07] |
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 | 7.05692e+01 | |||
| Coefficient B | 2.56630e-01 | |||
| Coefficient C | 6.63000e+02 | |||
| Coefficient D | 2.95500e-01 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 638.07 | |||
| ρl | 942.22 | kg/m3 | 189.26 | Calculated Property |
| ρl | 905.44 | kg/m3 | 239.13 | Calculated Property |
| ρl | 867.09 | kg/m3 | 289.00 | Calculated Property |
| ρl | 826.83 | kg/m3 | 338.86 | Calculated Property |
| ρl | 784.13 | kg/m3 | 388.73 | Calculated Property |
| ρl | 738.22 | kg/m3 | 438.60 | Calculated Property |
| ρl | 687.84 | kg/m3 | 488.47 | Calculated Property |
| ρl | 630.67 | kg/m3 | 538.33 | Calculated Property |
| ρl | 561.42 | kg/m3 | 588.20 | Calculated Property |
| ρl | 460.63 | kg/m3 | 638.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 6.28e-04] | N/m | [189.26; 638.07] |
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 | -8.09430e-03 | |||
| Coefficient B | 3.92070e+01 | |||
| Coefficient C | -3.11140e+00 | |||
| Coefficient D | 2.85030e-04 | |||
| Coefficient E | -4.60240e-06 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 638.07 | |||
| γ | 0.04 | N/m | 189.26 | Calculated Property |
| γ | 0.04 | N/m | 239.13 | Calculated Property |
| γ | 0.03 | N/m | 289.00 | Calculated Property |
| γ | 0.02 | N/m | 338.86 | Calculated Property |
| γ | 0.02 | N/m | 388.73 | Calculated Property |
| γ | 0.01 | N/m | 438.60 | Calculated Property |
| γ | 0.01 | N/m | 488.47 | Calculated Property |
| γ | 0.01 | N/m | 538.33 | Calculated Property |
| γ | 0.00 | N/m | 588.20 | Calculated Property |
| γ | 6.28e-04 | N/m | 638.07 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λgas | [0.00; 0.07] | W/m×K | [189.26; 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 | 2.54070e-01 | |||
| Coefficient B | -3.90160e-02 | |||
| Coefficient C | -2.16190e+02 | |||
| Coefficient D | 1.83240e+06 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 1000.00 | |||
| λgas | 0.00 | W/m×K | 189.26 | Calculated Property |
| λgas | 0.01 | W/m×K | 279.34 | Calculated Property |
| λgas | 0.01 | W/m×K | 369.42 | Calculated Property |
| λgas | 0.02 | W/m×K | 459.51 | Calculated Property |
| λgas | 0.03 | W/m×K | 549.59 | Calculated Property |
| λgas | 0.04 | W/m×K | 639.67 | Calculated Property |
| λgas | 0.05 | W/m×K | 729.75 | Calculated Property |
| λgas | 0.06 | W/m×K | 819.84 | Calculated Property |
| λgas | 0.07 | W/m×K | 909.92 | 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 | [189.26; 454.29] |
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 | -5.63030e-02 | |||
| Coefficient B | 5.61940e+00 | |||
| Coefficient C | -1.54080e+00 | |||
| Coefficient D | -3.31180e-04 | |||
| Coefficient E | -1.08730e-06 | |||
| Temperature range, min. | 189.26 | |||
| Temperature range, max. | 454.29 | |||
| λliquid | 0.14 | W/m×K | 189.26 | Calculated Property |
| λliquid | 0.14 | W/m×K | 218.71 | Calculated Property |
| λliquid | 0.13 | W/m×K | 248.16 | Calculated Property |
| λliquid | 0.13 | W/m×K | 277.60 | Calculated Property |
| λliquid | 0.12 | W/m×K | 307.05 | Calculated Property |
| λliquid | 0.12 | W/m×K | 336.50 | Calculated Property |
| λliquid | 0.11 | W/m×K | 365.95 | Calculated Property |
| λliquid | 0.10 | W/m×K | 395.39 | Calculated Property |
| λliquid | 0.10 | W/m×K | 424.84 | Calculated Property |
| λliquid | 0.09 | W/m×K | 454.29 | Calculated Property |
Similar Compounds
Find more compounds similar to Benzene, 1,3-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).
- 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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