| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5340 | Relay (1.0) Calculated Property | |
| ΔfG° | -36.57 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | [-263.70; -176.90] | kJ/mol |
|
| ΔfH°gas | -263.70 | kJ/mol | NIST |
| ΔfH°gas | -176.90 | kJ/mol | NIST |
| ΔfusH° | 18.11 | kJ/mol | Joback Calculated Property |
| ΔsubH° | [82.80; 95.02] | kJ/mol |
|
| ΔsubH° | 82.80 ± 0.30 | kJ/mol | NIST |
| ΔsubH° | 95.00 | kJ/mol | NIST |
| ΔsubH° | 95.02 | kJ/mol | NIST |
| ΔsubH° | 93.10 | kJ/mol | NIST |
| ΔvapH° | 74.43 | kJ/mol | Relay (1.0) Calculated Property |
| IE | 8.00 | eV | NIST |
| log10WS | [-2.05; -2.05] |
|
|
| log10WS | -2.05 | Aq. Solubility Prediction | |
| log10WS | -2.05 | Estimated Solubility | |
| logPoct/wat | 2.317 | Crippen Calculated Property | |
| McVol | 119.780 | ml/mol | McGowan Calculated Property |
| Pc | 3754.57 | kPa | Joback Calculated Property |
| Inp | [202.50; 1229.00] |
|
|
| Inp | 1220.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1202.50 | NIST | |
| Inp | 1201.60 | NIST | |
| Inp | 1199.10 | NIST | |
| Inp | 1202.50 | NIST | |
| Inp | 1204.10 | NIST | |
| Inp | 1199.10 | NIST | |
| Inp | 1202.50 | NIST | |
| Inp | 1204.10 | NIST | |
| Inp | 1202.50 | NIST | |
| Inp | 1201.60 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1211.00 | NIST | |
| Inp | 1212.90 | NIST | |
| Inp | 1215.80 | NIST | |
| Inp | 1229.00 | NIST | |
| Inp | 1226.00 | NIST | |
| Inp | 1171.00 | NIST | |
| Inp | 1174.00 | NIST | |
| Inp | 1184.00 | NIST | |
| Inp | 1173.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | 1205.00 | NIST | |
| Inp | 1204.00 | NIST | |
| Inp | Outlier 203.83 | NIST | |
| Inp | Outlier 202.50 | NIST | |
| Inp | Outlier 203.59 | NIST | |
| Inp | 1202.50 | NIST | |
| Inp | 1199.10 | NIST | |
| Inp | 1204.00 | NIST | |
| Tboil | [493.20; 494.15] | K |
|
| Tboil | 493.20 | K | NIST |
| Tboil | 494.15 ± 3.00 | K | NIST |
| Tc | 715.87 | K | Relay (1.0) Calculated Property |
| Tfus | [341.15; 346.15] | K |
|
| Tfus | 346.15 | K | Liquid pharmaceuticals formulation by eutectic formation |
| Tfus | 345.65 | K | Aq. Solubility Prediction |
| Tfus | 343.65 ± 2.00 | K | NIST |
| Tfus | 343.90 ± 2.00 | K | NIST |
| Tfus | 344.55 ± 2.00 | K | NIST |
| Tfus | 345.40 ± 3.00 | K | NIST |
| Tfus | 345.45 ± 1.50 | K | NIST |
| Tfus | 345.25 ± 2.00 | K | NIST |
| Tfus | Outlier 341.15 ± 4.00 | K | NIST |
| Tfus | 345.65 ± 2.00 | K | NIST |
| Tfus | 344.15 ± 2.00 | K | NIST |
| Tfus | 342.15 ± 2.00 | K | NIST |
| Vc | 0.423 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [266.84; 329.57] | J/mol×K | [522.78; 747.44] | |
| Cp,gas | 266.84 | J/mol×K | 522.78 | Joback Calculated Property |
| Cp,gas | 279.01 | J/mol×K | 560.22 | Joback Calculated Property |
| Cp,gas | 290.40 | J/mol×K | 597.67 | Joback Calculated Property |
| Cp,gas | 301.09 | J/mol×K | 635.11 | Joback Calculated Property |
| Cp,gas | 311.14 | J/mol×K | 672.55 | Joback Calculated Property |
| Cp,gas | 320.61 | J/mol×K | 709.99 | Joback Calculated Property |
| Cp,gas | 329.57 | J/mol×K | 747.44 | Joback Calculated Property |
| η | [0.0000660; 0.0017439] | Pa×s | [354.37; 522.78] | |
| η | 0.0017439 | Pa×s | 354.37 | Joback Calculated Property |
| η | 0.0008271 | Pa×s | 382.44 | Joback Calculated Property |
| η | 0.0004344 | Pa×s | 410.51 | Joback Calculated Property |
| η | 0.0002478 | Pa×s | 438.57 | Joback Calculated Property |
| η | 0.0001512 | Pa×s | 466.64 | Joback Calculated Property |
| η | 0.0000976 | Pa×s | 494.71 | Joback Calculated Property |
| η | 0.0000660 | Pa×s | 522.78 | Joback Calculated Property |
| ΔvapH | 53.20 | kJ/mol | 430.50 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.24; 202.66] | kPa | [345.15; 522.40] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.54349e+01 | |||
| Coefficient B | -4.49407e+03 | |||
| Coefficient C | -7.84680e+01 | |||
| Temperature range, min. | 345.15 | |||
| Temperature range, max. | 522.40 | |||
| Pvap | 0.24 | kPa | 345.15 | Calculated Property |
| Pvap | 0.77 | kPa | 364.84 | Calculated Property |
| Pvap | 2.12 | kPa | 384.54 | Calculated Property |
| Pvap | 5.15 | kPa | 404.23 | Calculated Property |
| Pvap | 11.31 | kPa | 423.93 | Calculated Property |
| Pvap | 22.82 | kPa | 443.62 | Calculated Property |
| Pvap | 42.84 | kPa | 463.32 | Calculated Property |
| Pvap | 75.63 | kPa | 483.01 | Calculated Property |
| Pvap | 126.67 | kPa | 502.71 | Calculated Property |
| Pvap | 202.66 | kPa | 522.40 | Calculated Property |
| Pvap | [1.32; 103.94] | kPa | [367.15; 494.15] |
KDB Vapor Pressure Data
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 6.88733e+01 | |||
| Coefficient B | -8.88021e+03 | |||
| Coefficient C | -7.60503e+00 | |||
| Coefficient D | 3.74291e-06 | |||
| Temperature range, min. | 367.15 | |||
| Temperature range, max. | 494.15 | |||
| Pvap | 1.32 | kPa | 367.15 | Calculated Property |
| Pvap | 2.52 | kPa | 381.26 | Calculated Property |
| Pvap | 4.58 | kPa | 395.37 | Calculated Property |
| Pvap | 7.93 | kPa | 409.48 | Calculated Property |
| Pvap | 13.20 | kPa | 423.59 | Calculated Property |
| Pvap | 21.16 | kPa | 437.71 | Calculated Property |
| Pvap | 32.83 | kPa | 451.82 | Calculated Property |
| Pvap | 49.46 | kPa | 465.93 | Calculated Property |
| Pvap | 72.56 | kPa | 480.04 | Calculated Property |
| Pvap | 103.94 | kPa | 494.15 | Calculated Property |
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