| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.7584 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-1358.00; -1355.20] | kJ/mol |
|
| ΔcH°solid | -1355.20 ± 0.67 | kJ/mol | NIST |
| ΔcH°solid | -1358.00 | kJ/mol | NIST |
| ΔcH°solid | -1356.20 | kJ/mol | NIST |
| ΔfG° | -468.46 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -727.43 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°liquid | -787.30 ± 1.70 | kJ/mol | NIST |
| ΔfH°solid | [-790.57; -787.76] | kJ/mol |
|
| ΔfH°solid | -790.57 ± 0.71 | kJ/mol | NIST |
| ΔfH°solid | -787.76 | kJ/mol | NIST |
| ΔfH°solid | -789.52 | kJ/mol | NIST |
| ΔfusH° | 27.28 | kJ/mol | Thermal analysis of phase change materials in the temperature range 120.150 .C |
| ΔvapH° | 92.94 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 10.71 | eV | Relay (1.0) Calculated Property |
| log10WS | -0.63 | Relay (1.0) Calculated Property | |
| logPoct/wat | -0.288 | Crippen Calculated Property | |
| McVol | 77.800 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 1 | KDB | |
| NFPA Health | 3 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | 6503.64 | kPa | Joback Calculated Property |
| S°solid,1 bar | 159.40 | J/mol×K | NIST |
| Tboil | 509.89 | K | Relay (1.0) Calculated Property |
| Tc | 616.00 ± 50.00 | K | NIST |
| Tfus | [402.90; 416.65] | K |
|
| Tfus | 402.90 ± 0.60 | K | NIST |
| Tfus | 403.80 ± 0.50 | K | NIST |
| Tfus | 416.65 ± 0.50 | K | NIST |
| Tfus | 405.00 ± 2.00 | K | NIST |
| Tfus | 403.40 ± 0.60 | K | NIST |
| Vc | 0.263 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [168.01; 191.01] | J/mol×K | [587.18; 769.82] | |
| Cp,gas | 168.01 | J/mol×K | 587.18 | Joback Calculated Property |
| Cp,gas | 172.46 | J/mol×K | 617.62 | Joback Calculated Property |
| Cp,gas | 176.64 | J/mol×K | 648.06 | Joback Calculated Property |
| Cp,gas | 180.57 | J/mol×K | 678.50 | Joback Calculated Property |
| Cp,gas | 184.27 | J/mol×K | 708.94 | Joback Calculated Property |
| Cp,gas | 187.74 | J/mol×K | 739.38 | Joback Calculated Property |
| Cp,gas | 191.01 | J/mol×K | 769.82 | Joback Calculated Property |
| Cp,solid | 135.60 | J/mol×K | 294.40 | NIST |
| η | [0.0000492; 0.0094225] | Pa×s | [351.26; 587.18] | |
| η | 0.0094225 | Pa×s | 351.26 | Joback Calculated Property |
| η | 0.0025249 | Pa×s | 390.58 | Joback Calculated Property |
| η | 0.0008609 | Pa×s | 429.90 | Joback Calculated Property |
| η | 0.0003515 | Pa×s | 469.22 | Joback Calculated Property |
| η | 0.0001649 | Pa×s | 508.54 | Joback Calculated Property |
| η | 0.0000862 | Pa×s | 547.86 | Joback Calculated Property |
| η | 0.0000492 | Pa×s | 587.18 | Joback Calculated Property |
| ΔfusH | 26.90 | kJ/mol | 411.90 | NIST |
| ΔsubH | [105.40; 110.00] | kJ/mol | [362.00; 368.50] | |
| ΔsubH | 110.00 ± 2.50 | kJ/mol | 362.00 | NIST |
| ΔsubH | 110.00 ± 3.00 | kJ/mol | 363.00 | NIST |
| ΔsubH | 109.00 ± 4.20 | kJ/mol | 363.50 | NIST |
| ΔsubH | 105.40 ± 1.70 | kJ/mol | 368.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.10; 4947.87] | kPa | [403.45; 773.00] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.80781e+02 | |||
| Coefficient B | -1.91037e+04 | |||
| Coefficient C | -2.28200e+01 | |||
| Coefficient D | 7.02669e-06 | |||
| Temperature range, min. | 403.45 | |||
| Temperature range, max. | 773.00 | |||
| Pvap | 0.10 | kPa | 403.45 | Calculated Property |
| Pvap | 1.06 | kPa | 444.51 | Calculated Property |
| Pvap | 7.00 | kPa | 485.57 | Calculated Property |
| Pvap | 31.60 | kPa | 526.63 | Calculated Property |
| Pvap | 107.70 | kPa | 567.69 | Calculated Property |
| Pvap | 297.38 | kPa | 608.76 | Calculated Property |
| Pvap | 700.34 | kPa | 649.82 | Calculated Property |
| Pvap | 1461.77 | kPa | 690.88 | Calculated Property |
| Pvap | 2784.00 | kPa | 731.94 | Calculated Property |
| Pvap | 4947.87 | kPa | 773.00 | Calculated Property |
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