| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2460 | Relay (1.0) Calculated Property | |
| ΔfG° | 40.92 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -47.84 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 10.52 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [35.40; 40.67] | kJ/mol |
|
| ΔvapH° | 40.67 | kJ/mol | NIST |
| ΔvapH° | 40.30 | kJ/mol | NIST |
| ΔvapH° | 39.70 | kJ/mol | NIST |
| ΔvapH° | 40.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 40.63 ± 0.04 | kJ/mol | NIST |
| ΔvapH° | Outlier 35.40 ± 0.04 | kJ/mol | NIST |
| IE | [9.21; 9.50] | eV |
|
| IE | 9.23 ± 0.01 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.24 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.23 ± 0.01 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.21 ± 0.01 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | Outlier 9.50 | eV | NIST |
| log10WS | [-2.96; -2.96] |
|
|
| log10WS | -2.96 | Aq. Solubility Prediction | |
| log10WS | -2.96 | Estimated Solubility | |
| logPoct/wat | 2.221 | Crippen Calculated Property | |
| McVol | 93.040 | ml/mol | McGowan Calculated Property |
| Pc | 3791.65 | kPa | Joback Calculated Property |
| Inp | [797.00; 844.90] |
|
|
| Inp | 810.00 | NIST | |
| Inp | Outlier 844.90 | NIST | |
| Inp | 821.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 814.00 | NIST | |
| Inp | 819.30 | NIST | |
| Inp | 806.20 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 810.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 813.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 826.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 820.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 809.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | Outlier 840.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | Outlier 840.00 | NIST | |
| Inp | 806.20 | NIST | |
| Inp | 798.00 | NIST | |
| Inp | 816.00 | NIST | |
| I | [1062.00; 1115.00] |
|
|
| I | Outlier 1111.00 | NIST | |
| I | 1069.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1067.00 | NIST | |
| I | 1062.00 | NIST | |
| I | 1063.00 | NIST | |
| I | 1066.00 | NIST | |
| I | Outlier 1115.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1065.00 | NIST | |
| I | 1062.00 | NIST | |
| I | 1065.00 | NIST | |
| Tboil | [399.00; 404.00] | K |
|
| Tboil | 403.55 | K | KDB |
| Tboil | 403.70 | K | NIST |
| Tboil | 403.70 | K | NIST |
| Tboil | 404.00 ± 2.00 | K | NIST |
| Tboil | 403.15 ± 4.00 | K | NIST |
| Tboil | 403.55 ± 0.50 | K | NIST |
| Tboil | 403.55 ± 0.40 | K | NIST |
| Tboil | Outlier 399.00 ± 4.00 | K | NIST |
| Tboil | 403.70 ± 0.50 | K | NIST |
| Tboil | 403.85 ± 0.30 | K | NIST |
| Tboil | 403.05 ± 0.50 | K | NIST |
| Tc | 614.10 | K | Relay (1.0) Calculated Property |
| Tfus | [143.15; 169.65] | K |
|
| Tfus | 143.15 | K | KDB |
| Tfus | 169.65 ± 0.30 | K | NIST |
| Vc | 0.349 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [107.41; 234.86] | J/mol×K | [273.00; 1000.00] |
Joback Predicted correlation
|
| Equation | Y = A + B·T + C·T² + D·T³ + E·T⁴ Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.09430e+01 | |||
| Coefficient B | 4.22820e-01 | |||
| Coefficient C | -2.75200e-04 | |||
| Coefficient D | 7.63000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 107.41 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 129.46 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 148.97 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 166.19 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 181.36 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 194.72 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 206.50 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 216.96 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 226.34 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 234.86 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0210395; 0.0003366] | Pa×s | [156.40; 412.00] |
Joback Predicted correlation
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -1.05270e+01 | |||
| Coefficient B | 1.04250e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 156.40 | |||
| Temperature range, max. | 412.00 | |||
| η | 0.0210395 | Pa×s | 156.40 | Calculated Property |
| η | 0.0075536 | Pa×s | 184.80 | Calculated Property |
| η | 0.0035628 | Pa×s | 213.20 | Calculated Property |
| η | 0.0020052 | Pa×s | 241.60 | Calculated Property |
| η | 0.0012736 | Pa×s | 270.00 | Calculated Property |
| η | 0.0008820 | Pa×s | 298.40 | Calculated Property |
| η | 0.0006510 | Pa×s | 326.80 | Calculated Property |
| η | 0.0005045 | Pa×s | 355.20 | Calculated Property |
| η | 0.0004059 | Pa×s | 383.60 | Calculated Property |
| η | 0.0003366 | Pa×s | 412.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [294.88; 429.64] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.46268e+01 | |||
| Coefficient B | -3.58287e+03 | |||
| Coefficient C | -4.50160e+01 | |||
| Temperature range, min. | 294.88 | |||
| Temperature range, max. | 429.64 | |||
| Pvap | 1.33 | kPa | 294.88 | Calculated Property |
| Pvap | 3.00 | kPa | 309.85 | Calculated Property |
| Pvap | 6.19 | kPa | 324.83 | Calculated Property |
| Pvap | 11.85 | kPa | 339.80 | Calculated Property |
| Pvap | 21.33 | kPa | 354.77 | Calculated Property |
| Pvap | 36.36 | kPa | 369.75 | Calculated Property |
| Pvap | 59.13 | kPa | 384.72 | Calculated Property |
| Pvap | 92.30 | kPa | 399.69 | Calculated Property |
| Pvap | 138.96 | kPa | 414.67 | Calculated Property |
| Pvap | 202.66 | kPa | 429.64 | Calculated Property |
| Pvap | [1.32; 198.11] | kPa | [292.15; 431.15] |
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 | 9.36261e+01 | |||
| Coefficient B | -7.91214e+03 | |||
| Coefficient C | -1.18026e+01 | |||
| Coefficient D | 8.68183e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 292.15 | |||
| Temperature range, max. | 431.15 | |||
| Pvap | 1.32 | kPa | 292.15 | Calculated Property |
| Pvap | 3.04 | kPa | 307.59 | Calculated Property |
| Pvap | 6.34 | kPa | 323.04 | Calculated Property |
| Pvap | 12.20 | kPa | 338.48 | Calculated Property |
| Pvap | 21.93 | kPa | 353.93 | Calculated Property |
| Pvap | 37.17 | kPa | 369.37 | Calculated Property |
| Pvap | 59.91 | kPa | 384.82 | Calculated Property |
| Pvap | 92.48 | kPa | 400.26 | Calculated Property |
| Pvap | 137.55 | kPa | 415.71 | Calculated Property |
| Pvap | 198.11 | kPa | 431.15 | Calculated Property |
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