| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2370; 0.3359] |
|
|
| ω | 0.2384 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| ω | 0.3359 | Passut and Danner (1973), critical constants and acentric factors Compiled value | |
| ω | 0.2370 | KDB | |
| ΔcH°liquid | [-4598.90; -4586.50] | kJ/mol |
|
| ΔcH°liquid | -4597.00 ± 0.80 | kJ/mol | NIST |
| ΔcH°liquid | -4597.60 ± 0.60 | kJ/mol | NIST |
| ΔcH°liquid | -4598.90 ± 1.70 | kJ/mol | NIST |
| ΔcH°liquid | -4586.50 | kJ/mol | NIST |
| ΔfG° | 63.05 | kJ/mol | KDB |
| Δc,grossH | 4597.80 | kJ/mol | KDB |
| Δc,netH | 4289.856 | kJ/mol | KDB |
| ΔfH°gas | -119.40 | kJ/mol | KDB |
| ΔfH°liquid | -156.40 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 2.55 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [37.00; 39.40] | kJ/mol |
|
| ΔvapH° | 38.50 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 39.40 | kJ/mol | NIST |
| ΔvapH° | Outlier 37.00 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 2.10 | kJ/mol | NIST |
| ΔvapH° | 38.50 ± 0.20 | kJ/mol | NIST |
| IE | [9.82; 9.97] | eV |
|
| IE | 9.90 ± 0.10 | eV | NIST |
| IE | 9.82 ± 0.05 | eV | NIST |
| IE | 9.96 | eV | NIST |
| IE | 9.97 | eV | NIST |
| IE | 9.88 ± 0.05 | eV | NIST |
| log10WS | [-3.52; -3.51] |
|
|
| log10WS | -3.52 | Aq. Solubility Prediction | |
| log10WS | -3.51 | Estimated Solubility | |
| logPoct/wat | 2.731 | Crippen Calculated Property | |
| McVol | 98.630 | ml/mol | McGowan Calculated Property |
| Pc | [3723.17; 3826.00] | kPa |
|
| Pc | 3820.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Pc | 3819.95 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | Outlier 3723.17 | kPa | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Pc | 3820.00 | kPa | KDB |
| Pc | 3820.00 ± 40.00 | kPa | NIST |
| Pc | 3813.00 ± 50.00 | kPa | NIST |
| Pc | 3826.00 ± 40.53 | kPa | NIST |
| ρc | 277.87 ± 3.93 | kg/m3 | NIST |
| Inp | [784.00; 846.00] |
|
|
| Inp | 787.00 | NIST | |
| Inp | Outlier 837.50 | NIST | |
| Inp | Outlier 836.00 | NIST | |
| Inp | Outlier 837.00 | NIST | |
| Inp | 794.20 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 806.90 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 788.00 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 815.00 | NIST | |
| Inp | 811.60 | NIST | |
| Inp | 791.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 829.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 784.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 795.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 806.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 804.00 | NIST | |
| Inp | 824.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 787.00 | NIST | |
| Inp | 794.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 796.00 | NIST | |
| Inp | 790.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | Outlier 846.00 | NIST | |
| Inp | 803.00 | NIST | |
| Inp | 797.00 | NIST | |
| Inp | 807.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 786.00 | NIST | |
| Inp | Outlier 837.50 | NIST | |
| Inp | 806.90 | NIST | |
| Inp | 789.00 | NIST | |
| Inp | 811.00 | NIST | |
| Inp | 812.00 | NIST | |
| Inp | 816.00 | NIST | |
| Inp | 800.00 | NIST | |
| Inp | 819.00 | NIST | |
| Inp | 796.00 | NIST | |
| Ip | [878.00; 899.00] |
|
|
| Ip | 899.00 | NIST | |
| Ip | 878.00 | NIST | |
| Ip | 892.00 | NIST | |
| Ip | 883.00 | NIST | |
| Ip | 899.00 | NIST | |
| Ip | 883.00 | NIST | |
| S°gas | 342.30 ± 1.30 | J/mol×K | NIST |
| S°liquid | 242.55 | J/mol×K | NIST |
| Tboil | [391.25; 393.00] | K |
|
| Tboil | 391.63 | K | KDB |
| Tboil | 391.70 | K | NIST |
| Tboil | Outlier 393.00 ± 2.00 | K | NIST |
| Tboil | 391.99 ± 0.20 | K | NIST |
| Tboil | 391.99 ± 0.30 | K | NIST |
| Tboil | 391.99 ± 0.30 | K | NIST |
| Tboil | 391.63 ± 0.30 | K | NIST |
| Tboil | 391.25 ± 0.60 | K | NIST |
| Tboil | 392.15 ± 2.00 | K | NIST |
| Tc | [589.26; 604.20] | K |
|
| Tc | 604.20 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Tc | 604.20 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | Outlier 589.26 | K | Passut and Danner (1973), critical constants and acentric factors Compiled value |
| Tc | 604.20 | K | KDB |
| Tc | 604.20 ± 0.50 | K | NIST |
| Tc | 604.20 ± 0.50 | K | NIST |
| Tfus | [260.95; 265.20] | K |
|
| Tfus | 265.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 265.12 | K | KDB |
| Tfus | 264.69 ± 0.25 | K | NIST |
| Tfus | 265.20 ± 2.00 | K | NIST |
| Tfus | 265.02 ± 0.06 | K | NIST |
| Tfus | 265.02 ± 0.04 | K | NIST |
| Tfus | 265.05 ± 0.02 | K | NIST |
| Tfus | Outlier 260.95 ± 0.30 | K | NIST |
| Ttriple | [265.00; 265.12] | K |
|
| Ttriple | 265.00 ± 0.07 | K | NIST |
| Ttriple | 265.12 ± 0.05 | K | NIST |
| Ttriple | 265.10 ± 3.00 | K | NIST |
| Ttriple | 265.00 ± 0.07 | K | NIST |
| Ttriple | 265.12 ± 0.05 | K | NIST |
| Vc | [0.353; 0.354] | m3/kmol |
|
| Vc | 0.353 | m3/kmol | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value |
| Vc | 0.353 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Vc | 0.353 | m3/kmol | KDB |
| Vc | 0.353 | m3/kmol | NIST |
| Vc | 0.354 ± 0.007 | m3/kmol | NIST |
| Zc | [0.2680000; 0.2684240] |
|
|
| Zc | 0.2680000 | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 5 Compiled value | |
| Zc | 0.2684240 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [108.70; 360.66] | 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 | -8.01400e+01 | |||
| Coefficient B | 8.07800e-01 | |||
| Coefficient C | -4.47000e-04 | |||
| Coefficient D | 8.00000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 108.70 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 153.24 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 193.05 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 228.39 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 259.50 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 286.66 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 310.09 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 330.07 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 346.84 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 360.66 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0017742; 0.0001985] | Pa×s | [265.04; 422.94] |
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 | -1.22011e+01 | |||
| Coefficient B | 1.55489e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Comment | Liquid phase. Joback/Reid (1987), valid from Tf to 0.7·Tc. | |||
| Temperature range, min. | 265.04 | |||
| Temperature range, max. | 422.94 | |||
| η | 0.0017742 | Pa×s | 265.04 | Calculated Property |
| η | 0.0012326 | Pa×s | 282.58 | Calculated Property |
| η | 0.0008936 | Pa×s | 300.13 | Calculated Property |
| η | 0.0006712 | Pa×s | 317.67 | Calculated Property |
| η | 0.0005195 | Pa×s | 335.22 | Calculated Property |
| η | 0.0004125 | Pa×s | 352.76 | Calculated Property |
| η | 0.0003347 | Pa×s | 370.31 | Calculated Property |
| η | 0.0002768 | Pa×s | 387.85 | Calculated Property |
| η | 0.0002327 | Pa×s | 405.40 | Calculated Property |
| η | 0.0001985 | Pa×s | 422.94 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.39; 202.67] | kPa | [265.12; 418.93] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.41291e+01 | |||
| Coefficient B | -3.26491e+03 | |||
| Coefficient C | -4.86550e+01 | |||
| Temperature range, min. | 265.12 | |||
| Temperature range, max. | 418.93 | |||
| Pvap | 0.39 | kPa | 265.12 | Calculated Property |
| Pvap | 1.16 | kPa | 282.21 | Calculated Property |
| Pvap | 3.01 | kPa | 299.30 | Calculated Property |
| Pvap | 6.92 | kPa | 316.39 | Calculated Property |
| Pvap | 14.39 | kPa | 333.48 | Calculated Property |
| Pvap | 27.53 | kPa | 350.57 | Calculated Property |
| Pvap | 49.13 | kPa | 367.66 | Calculated Property |
| Pvap | 82.67 | kPa | 384.75 | Calculated Property |
| Pvap | 132.28 | kPa | 401.84 | Calculated Property |
| Pvap | 202.67 | kPa | 418.93 | Calculated Property |
| Pvap | [0.39; 3831.50] | kPa | [265.12; 604.30] |
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 | 8.37466e+01 | |||
| Coefficient B | -7.38221e+03 | |||
| Coefficient C | -1.02752e+01 | |||
| Coefficient D | 6.91167e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 265.12 | |||
| Temperature range, max. | 604.30 | |||
| Pvap | 0.39 | kPa | 265.12 | Calculated Property |
| Pvap | 3.66 | kPa | 302.81 | Calculated Property |
| Pvap | 19.26 | kPa | 340.49 | Calculated Property |
| Pvap | 68.53 | kPa | 378.18 | Calculated Property |
| Pvap | 186.24 | kPa | 415.87 | Calculated Property |
| Pvap | 418.69 | kPa | 453.55 | Calculated Property |
| Pvap | 822.00 | kPa | 491.24 | Calculated Property |
| Pvap | 1463.67 | kPa | 528.93 | Calculated Property |
| Pvap | 2428.81 | kPa | 566.61 | Calculated Property |
| Pvap | 3831.50 | kPa | 604.30 | Calculated Property |
| Pvap | [19.88; 270.07] | kPa | [341.30; 432.17] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37628e+01 | |||
| Coefficient B | -3.06336e+03 | |||
| Coefficient C | -5.69460e+01 | |||
| Reference | Finke, Scott, et al., 1956 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 341.30 | |||
| Temperature range, max. | 432.17 | |||
| Pvap | 19.88 | kPa | 341.30 | Calculated Property |
| Pvap | 28.76 | kPa | 351.40 | Calculated Property |
| Pvap | 40.61 | kPa | 361.49 | Calculated Property |
| Pvap | 56.08 | kPa | 371.59 | Calculated Property |
| Pvap | 75.91 | kPa | 381.69 | Calculated Property |
| Pvap | 100.88 | kPa | 391.78 | Calculated Property |
| Pvap | 131.86 | kPa | 401.88 | Calculated Property |
| Pvap | 169.75 | kPa | 411.98 | Calculated Property |
| Pvap | 215.49 | kPa | 422.07 | Calculated Property |
| Pvap | 270.07 | kPa | 432.17 | Calculated Property |
| Pvap | [19.88; 270.07] | kPa | [341.30; 432.17] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.37628e+01 | |||
| Coefficient B | -3.06336e+03 | |||
| Coefficient C | -5.69460e+01 | |||
| Reference | Finke, Scott, et al., 1956, 3 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 341.30 | |||
| Temperature range, max. | 432.17 | |||
| Pvap | 19.88 | kPa | 341.30 | Calculated Property |
| Pvap | 28.76 | kPa | 351.40 | Calculated Property |
| Pvap | 40.61 | kPa | 361.49 | Calculated Property |
| Pvap | 56.08 | kPa | 371.59 | Calculated Property |
| Pvap | 75.91 | kPa | 381.69 | Calculated Property |
| Pvap | 100.88 | kPa | 391.78 | Calculated Property |
| Pvap | 131.86 | kPa | 401.88 | Calculated Property |
| Pvap | 169.75 | kPa | 411.98 | Calculated Property |
| Pvap | 215.49 | kPa | 422.07 | Calculated Property |
| Pvap | 270.07 | kPa | 432.17 | Calculated Property |
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