| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7404 | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value | |
| Tig | 633.15 | K | NCMS SOLV-DB |
| Tflash,cc | 380.15 | K | NCMS SOLV-DB |
| ΔfG° | -503.89 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -781.13 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfusH° | 23.22 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 91.21 | kJ/mol | NCMS SOLV-DB |
| IE | 9.54 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.21 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.714 | NCMS SOLV-DB | |
| McVol | 142.760 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | NCMS SOLV-DB | |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [2730.00; 2730.00] | kPa |
|
| Pc | 2730.00 | kPa | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Pc | 2730.00 | kPa | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Pc | 2730.00 ± 200.00 | kPa | NIST |
| Inp | [1147.00; 1184.00] |
|
|
| Inp | 1184.00 | NIST | |
| Inp | 1147.00 | NIST | |
| Inp | 1183.80 | NIST | |
| Inp | 1183.80 | NIST | |
| Tboil | [490.55; 491.70] | K |
|
| Tboil | 490.55 | K | NCMS SOLV-DB |
| Tboil | 491.70 | K | NIST |
| Tc | [663.00; 663.00] | K |
|
| Tc | 663.00 | K | IUPAC Vapor-Liquid Critical Properties of Elements and Compounds, part 7 Compiled value |
| Tc | 663.00 | K | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Tc | 663.00 ± 3.00 | K | NIST |
| Tfus | [248.15; 248.15] | K |
|
| Tfus | 248.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Tfus | 248.15 | K | NCMS SOLV-DB |
| Vc | 0.546 | m3/kmol | PSRK revision IV (2005), critical constants and acentric factors of 1000 components Compiled value |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [222.34; 477.17] | 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 | 7.20250e+01 | |||
| Coefficient B | 5.82640e-01 | |||
| Coefficient C | -9.48000e-05 | |||
| Coefficient D | -8.27000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 222.34 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 262.62 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 300.53 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 335.78 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 368.14 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 397.32 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 423.08 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 445.15 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 463.26 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 477.17 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [364.57; 519.55] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.67698e+01 | |||
| Coefficient B | -5.82618e+03 | |||
| Coefficient C | -1.10880e+01 | |||
| Temperature range, min. | 364.57 | |||
| Temperature range, max. | 519.55 | |||
| Pvap | 1.33 | kPa | 364.57 | Calculated Property |
| Pvap | 2.87 | kPa | 381.79 | Calculated Property |
| Pvap | 5.76 | kPa | 399.01 | Calculated Property |
| Pvap | 10.91 | kPa | 416.23 | Calculated Property |
| Pvap | 19.60 | kPa | 433.45 | Calculated Property |
| Pvap | 33.65 | kPa | 450.67 | Calculated Property |
| Pvap | 55.45 | kPa | 467.89 | Calculated Property |
| Pvap | 88.13 | kPa | 485.11 | Calculated Property |
| Pvap | 135.60 | kPa | 502.33 | Calculated Property |
| Pvap | 202.63 | kPa | 519.55 | Calculated Property |
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