| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.2670 | KDB | |
| ΔfG° | 78.93 | kJ/mol | Joback Calculated Property |
| Δc,grossH | 3986.18 | kJ/mol | KDB |
| Δc,netH | 3722.086 | kJ/mol | KDB |
| ΔfH°gas | -50.14 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 8.71 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [30.50; 30.50] | kJ/mol |
|
| ΔvapH° | 30.50 | kJ/mol | NIST |
| ΔvapH° | 30.50 | kJ/mol | NIST |
| ΔvapH° | 30.50 | kJ/mol | NIST |
| IE | [9.04; 9.08] | eV |
|
| IE | 9.08 ± 0.01 | eV | NIST |
| IE | 9.04 | eV | NIST |
| IE | 9.08 ± 0.01 | eV | NIST |
| log10WS | [-3.03; -3.03] |
|
|
| log10WS | -3.03 | Aq. Solubility Prediction | |
| log10WS | -3.03 | Estimated Solubility | |
| logPoct/wat | 2.363 | Crippen Calculated Property | |
| McVol | 91.100 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | 3280.00 | kPa | KDB |
| Inp | [575.00; 607.00] |
|
|
| Inp | 579.60 | NIST | |
| Inp | Outlier 600.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 579.40 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 580.10 | NIST | |
| Inp | 580.50 | NIST | |
| Inp | 590.70 | NIST | |
| Inp | 591.20 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 580.40 | NIST | |
| Inp | 587.50 | NIST | |
| Inp | 588.10 | NIST | |
| Inp | 580.30 | NIST | |
| Inp | 580.90 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 592.40 | NIST | |
| Inp | 592.50 | NIST | |
| Inp | 592.60 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 585.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 587.70 | NIST | |
| Inp | 588.10 | NIST | |
| Inp | 588.60 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 589.50 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 588.80 | NIST | |
| Inp | 588.30 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 587.60 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 580.10 | NIST | |
| Inp | 579.80 | NIST | |
| Inp | 580.30 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 580.20 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 579.25 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | Outlier 575.00 | NIST | |
| Inp | 590.20 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 584.20 | NIST | |
| Inp | 587.40 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 583.35 | NIST | |
| Inp | 583.43 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 579.60 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | Outlier 600.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | Outlier 607.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 590.20 | NIST | |
| Inp | 584.20 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 582.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 591.20 | NIST | |
| Inp | 587.50 | NIST | |
| Inp | 592.50 | NIST | |
| Inp | 587.70 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 580.30 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | Outlier 575.00 | NIST | |
| I | [623.00; 634.00] |
|
|
| I | 634.00 | NIST | |
| I | 623.00 | NIST | |
| I | 634.00 | NIST | |
| Tboil | [333.73; 338.15] | K |
|
| Tboil | 335.30 | K | KDB |
| Tboil | 335.30 | K | NIST |
| Tboil | 333.90 ± 0.70 | K | NIST |
| Tboil | 334.30 ± 0.60 | K | NIST |
| Tboil | 334.70 ± 2.00 | K | NIST |
| Tboil | 334.90 ± 0.40 | K | NIST |
| Tboil | 334.90 ± 0.20 | K | NIST |
| Tboil | 335.27 ± 0.20 | K | NIST |
| Tboil | 335.27 ± 0.20 | K | NIST |
| Tboil | 335.26 ± 0.20 | K | NIST |
| Tboil | 335.23 ± 0.20 | K | NIST |
| Tboil | 334.15 ± 1.00 | K | NIST |
| Tboil | 333.73 ± 0.50 | K | NIST |
| Tboil | 335.35 ± 0.30 | K | NIST |
| Tboil | 335.22 ± 0.20 | K | NIST |
| Tboil | 335.40 ± 0.30 | K | NIST |
| Tboil | 335.15 ± 0.20 | K | NIST |
| Tboil | 334.90 ± 0.60 | K | NIST |
| Tboil | 335.05 ± 0.50 | K | NIST |
| Tboil | 334.90 ± 0.60 | K | NIST |
| Tboil | Outlier 338.15 ± 2.00 | K | NIST |
| Tc | [506.50; 521.00] | K |
|
| Tc | 521.00 | K | Gas-Liquid Critical Temperatures of Some Alkenes, Amines, and Cyclic Hydrocarbons |
| Tc | 506.50 | K | KDB |
| Tfus | [137.00; 137.43] | K |
|
| Tfus | 137.00 | K | KDB |
| Tfus | 137.25 | K | Aq. Solubility Prediction |
| Tfus | 137.43 ± 0.40 | K | NIST |
| Vc | 0.353 | m3/kmol | KDB |
| Zc | 0.2753260 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [145.82; 200.57] | J/mol×K | [333.24; 503.41] | |
| Cp,gas | 145.82 | J/mol×K | 333.24 | Joback Calculated Property |
| Cp,gas | 155.88 | J/mol×K | 361.60 | Joback Calculated Property |
| Cp,gas | 165.55 | J/mol×K | 389.96 | Joback Calculated Property |
| Cp,gas | 174.84 | J/mol×K | 418.33 | Joback Calculated Property |
| Cp,gas | 183.77 | J/mol×K | 446.69 | Joback Calculated Property |
| Cp,gas | 192.34 | J/mol×K | 475.05 | Joback Calculated Property |
| Cp,gas | 200.57 | J/mol×K | 503.41 | Joback Calculated Property |
| ΔvapH | [28.07; 31.60] | kJ/mol | [306.50; 335.30] | |
| ΔvapH | 31.60 | kJ/mol | 306.50 | NIST |
| ΔvapH | 28.07 | kJ/mol | 335.30 | KDB |
| n0 | 1.38912 | 298.15 | KDB | |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [241.31; 358.95] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.40283e+01 | |||
| Coefficient B | -2.80476e+03 | |||
| Coefficient C | -3.71870e+01 | |||
| Temperature range, min. | 241.31 | |||
| Temperature range, max. | 358.95 | |||
| Pvap | 1.33 | kPa | 241.31 | Calculated Property |
| Pvap | 3.05 | kPa | 254.38 | Calculated Property |
| Pvap | 6.35 | kPa | 267.45 | Calculated Property |
| Pvap | 12.21 | kPa | 280.52 | Calculated Property |
| Pvap | 21.97 | kPa | 293.59 | Calculated Property |
| Pvap | 37.34 | kPa | 306.67 | Calculated Property |
| Pvap | 60.44 | kPa | 319.74 | Calculated Property |
| Pvap | 93.74 | kPa | 332.81 | Calculated Property |
| Pvap | 140.09 | kPa | 345.88 | Calculated Property |
| Pvap | 202.64 | kPa | 358.95 | Calculated Property |
| Pvap | [8.72e-07; 3159.39] | kPa | [137.42; 507.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.36898e+01 | |||
| Coefficient B | -6.02144e+03 | |||
| Coefficient C | -8.92966e+00 | |||
| Coefficient D | 7.24925e-06 | |||
| Temperature range, min. | 137.42 | |||
| Temperature range, max. | 507.00 | |||
| Pvap | 8.72e-07 | kPa | 137.42 | Calculated Property |
| Pvap | 2.22e-03 | kPa | 178.48 | Calculated Property |
| Pvap | 0.22 | kPa | 219.55 | Calculated Property |
| Pvap | 4.06 | kPa | 260.61 | Calculated Property |
| Pvap | 30.18 | kPa | 301.68 | Calculated Property |
| Pvap | 127.83 | kPa | 342.74 | Calculated Property |
| Pvap | 378.51 | kPa | 383.81 | Calculated Property |
| Pvap | 885.04 | kPa | 424.87 | Calculated Property |
| Pvap | 1765.18 | kPa | 465.94 | Calculated Property |
| Pvap | 3159.39 | kPa | 507.00 | Calculated Property |
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