Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4050 | KDB | |
ΔcH°liquid | [-5855.80; -5853.00] | kJ/mol | |
ΔcH°liquid | -5855.80 ± 1.10 | kJ/mol | NIST |
ΔcH°liquid | -5853.00 ± 2.60 | kJ/mol | NIST |
ΔfG° | 126.47 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -36.14 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | [-83.00; -80.10] | kJ/mol | |
ΔfH°liquid | -80.10 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -83.00 ± 2.60 | kJ/mol | NIST |
ΔfusH° | 14.92 | kJ/mol | Joback Calculated Property |
ΔvapH° | 53.90 | kJ/mol | NIST |
log10WS | -3.23 | Crippen Calculated Property | |
logPoct/wat | 2.866 | Crippen Calculated Property | |
McVol | 128.000 | ml/mol | McGowan Calculated Property |
Pc | 2929.00 | kPa | KDB |
Inp | [1029.00; 1120.00] | ||
Inp | 1081.60 | NIST | |
Inp | 1084.70 | NIST | |
Inp | 1078.00 | NIST | |
Inp | 1069.60 | NIST | |
Inp | 1064.97 | NIST | |
Inp | 1070.40 | NIST | |
Inp | 1072.00 | NIST | |
Inp | 1099.20 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1105.00 | NIST | |
Inp | 1080.75 | NIST | |
Inp | 1082.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | Outlier 1120.00 | NIST | |
Inp | 1081.80 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1072.10 | NIST | |
Inp | 1075.70 | NIST | |
Inp | 1076.00 | NIST | |
Inp | 1073.00 | NIST | |
Inp | 1082.00 | NIST | |
Inp | 1075.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1061.00 | NIST | |
Inp | 1086.00 | NIST | |
Inp | 1082.00 | NIST | |
Inp | Outlier 1032.00 | NIST | |
Inp | Outlier 1029.00 | NIST | |
Inp | Outlier 1029.00 | NIST | |
Inp | 1074.00 | NIST | |
Inp | 1075.00 | NIST | |
Inp | 1097.10 | NIST | |
Inp | 1062.00 | NIST | |
Inp | 1072.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1081.00 | NIST | |
Inp | 1086.00 | NIST | |
Inp | 1080.00 | NIST | |
Inp | 1070.00 | NIST | |
Inp | 1086.00 | NIST | |
Inp | 1074.00 | NIST | |
I | [1347.50; 1372.10] | ||
I | 1372.10 | NIST | |
I | 1347.50 | NIST | |
I | 1363.00 | NIST | |
I | 1348.00 | NIST | |
I | 1372.00 | NIST | |
I | 1348.00 | NIST | |
I | 1372.00 | NIST | |
I | 1355.00 | NIST | |
I | 1363.00 | NIST | |
I | 1348.00 | NIST | |
I | 1372.10 | NIST | |
Tboil | [456.90; 463.20] | K | |
Tboil | Outlier 456.90 | K | KDB |
Tboil | 463.20 | K | NIST |
Tboil | 463.16 ± 0.20 | K | NIST |
Tboil | 463.20 ± 1.00 | K | NIST |
Tboil | 463.10 ± 0.20 | K | NIST |
Tboil | 463.10 ± 0.30 | K | NIST |
Tboil | 463.10 ± 0.15 | K | NIST |
Tboil | 463.16 ± 0.20 | K | NIST |
Tboil | 463.10 ± 0.30 | K | NIST |
Tc | 665.10 | K | KDB |
Tfus | 256.81 ± 0.20 | K | NIST |
Vc | 0.446 | m3/kmol | KDB |
Zc | 0.2363340 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [258.11; 333.41] | J/mol×K | [464.84; 672.09] | |
Cp,gas | 258.11 | J/mol×K | 464.84 | Joback Calculated Property |
Cp,gas | 272.33 | J/mol×K | 499.38 | Joback Calculated Property |
Cp,gas | 285.86 | J/mol×K | 533.92 | Joback Calculated Property |
Cp,gas | 298.71 | J/mol×K | 568.47 | Joback Calculated Property |
Cp,gas | 310.90 | J/mol×K | 603.01 | Joback Calculated Property |
Cp,gas | 322.46 | J/mol×K | 637.55 | Joback Calculated Property |
Cp,gas | 333.41 | J/mol×K | 672.09 | Joback Calculated Property |
η | [0.0002068; 0.0017125] | Pa×s | [253.92; 464.84] | |
η | 0.0017125 | Pa×s | 253.92 | Joback Calculated Property |
η | 0.0009718 | Pa×s | 289.07 | Joback Calculated Property |
η | 0.0006236 | Pa×s | 324.23 | Joback Calculated Property |
η | 0.0004364 | Pa×s | 359.38 | Joback Calculated Property |
η | 0.0003255 | Pa×s | 394.53 | Joback Calculated Property |
η | 0.0002547 | Pa×s | 429.69 | Joback Calculated Property |
η | 0.0002068 | Pa×s | 464.84 | Joback Calculated Property |
ΔvapH | [48.60; 48.80] | kJ/mol | [380.00; 417.00] | |
ΔvapH | 48.60 | kJ/mol | 380.00 | NIST |
ΔvapH | 48.80 | kJ/mol | 417.00 | NIST |
ρl | 885.86 | kg/m3 | 293.10 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [341.33; 493.26] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45844e+01 | |||
Coefficient B | -4.00908e+03 | |||
Coefficient C | -6.09150e+01 | |||
Temperature range, min. | 341.33 | |||
Temperature range, max. | 493.26 | |||
Pvap | 1.33 | kPa | 341.33 | Calculated Property |
Pvap | 3.00 | kPa | 358.21 | Calculated Property |
Pvap | 6.20 | kPa | 375.09 | Calculated Property |
Pvap | 11.88 | kPa | 391.97 | Calculated Property |
Pvap | 21.37 | kPa | 408.85 | Calculated Property |
Pvap | 36.42 | kPa | 425.74 | Calculated Property |
Pvap | 59.22 | kPa | 442.62 | Calculated Property |
Pvap | 92.39 | kPa | 459.50 | Calculated Property |
Pvap | 139.03 | kPa | 476.38 | Calculated Property |
Pvap | 202.65 | kPa | 493.26 | Calculated Property |
Pvap | [2.83e-03; 3015.06] | kPa | [256.89; 671.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.01218e+02 | |||
Coefficient B | -9.75905e+03 | |||
Coefficient C | -1.25287e+01 | |||
Coefficient D | 6.40530e-06 | |||
Temperature range, min. | 256.89 | |||
Temperature range, max. | 671.00 | |||
Pvap | 2.83e-03 | kPa | 256.89 | Calculated Property |
Pvap | 0.14 | kPa | 302.90 | Calculated Property |
Pvap | 1.96 | kPa | 348.91 | Calculated Property |
Pvap | 13.47 | kPa | 394.93 | Calculated Property |
Pvap | 57.10 | kPa | 440.94 | Calculated Property |
Pvap | 175.21 | kPa | 486.95 | Calculated Property |
Pvap | 430.76 | kPa | 532.96 | Calculated Property |
Pvap | 907.78 | kPa | 578.98 | Calculated Property |
Pvap | 1717.59 | kPa | 624.99 | Calculated Property |
Pvap | 3015.06 | kPa | 671.00 | Calculated Property |
Find more compounds similar to Benzene, 2-ethyl-1,3-dimethyl-.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.