| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3111 | Relay (1.0) Calculated Property | |
| ΔcH°liquid | -3485.00 ± 2.10 | kJ/mol | NIST |
| ΔfG° | -59.35 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -155.00 ± 2.70 | kJ/mol | NIST |
| ΔfusH° | 73.40 | kJ/mol | Experimental and Computational Studies on the Structural and Thermodynamic Properties of Two Sulfur Heterocyclic Keto Compounds |
| ΔsubH° | 72.60 ± 1.70 | kJ/mol | NIST |
| ΔvapH° | 72.63 | kJ/mol | NIST |
| IE | 8.90 ± 0.05 | eV | NIST |
| log10WS | 0.32 | Relay (1.0) Calculated Property | |
| logPoct/wat | 1.083 | Crippen Calculated Property | |
| McVol | 88.370 | ml/mol | McGowan Calculated Property |
| Pc | 4883.38 | kPa | Joback Calculated Property |
| Inp | [1011.00; 1017.00] |
|
|
| Inp | 1011.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1017.00 | NIST | |
| Inp | 1011.00 | NIST | |
| Tboil | 473.52 | K | Relay (1.0) Calculated Property |
| Tc | 734.84 | K | Relay (1.0) Calculated Property |
| Tfus | 335.15 | K | Jean-Claude Bradley Open Melting Point Dataset (2014, CC0) Compiled value |
| Vc | 0.287 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔsubH | 71.70 ± 1.70 | kJ/mol | 317.00 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [102.08; 281.16] | 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 | -1.49500e+01 | |||
| Coefficient B | 4.73510e-01 | |||
| Coefficient C | -1.59300e-04 | |||
| Coefficient D | -1.81000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 102.08 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 131.83 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 159.25 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 184.28 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 206.87 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 226.96 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 244.49 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 259.41 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 271.65 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 281.16 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.67] | kPa | [342.73; 487.19] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.72313e+01 | |||
| Coefficient B | -5.80715e+03 | |||
| Coefficient C | 0.00000e+00 | |||
| Temperature range, min. | 342.73 | |||
| Temperature range, max. | 487.19 | |||
| Pvap | 1.33 | kPa | 342.73 | Calculated Property |
| Pvap | 2.84 | kPa | 358.78 | Calculated Property |
| Pvap | 5.69 | kPa | 374.83 | Calculated Property |
| Pvap | 10.75 | kPa | 390.88 | Calculated Property |
| Pvap | 19.31 | kPa | 406.93 | Calculated Property |
| Pvap | 33.19 | kPa | 422.99 | Calculated Property |
| Pvap | 54.83 | kPa | 439.04 | Calculated Property |
| Pvap | 87.42 | kPa | 455.09 | Calculated Property |
| Pvap | 135.03 | kPa | 471.14 | Calculated Property |
| Pvap | 202.67 | kPa | 487.19 | Calculated Property |
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