| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3996 | Relay (1.0) Calculated Property | |
| ΔcH°solid | [-3603.80; -3588.00] | kJ/mol |
|
| ΔcH°solid | -3603.80 ± 1.50 | kJ/mol | NIST |
| ΔcH°solid | -3603.70 ± 0.84 | kJ/mol | NIST |
| ΔcH°solid | -3588.00 ± 6.30 | kJ/mol | NIST |
| ΔfG° | -15.18 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -239.60 | kJ/mol | NIST |
| ΔfH°solid | -329.40 ± 1.70 | kJ/mol | NIST |
| ΔfusH° | 16.16 | kJ/mol | Solid-Liquid Equilibrium and Activity Coefficients for Caprolactam + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide and Cyclohexanone Oxime + 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide |
| ΔsubH° | [87.30; 89.76] | kJ/mol |
|
| ΔsubH° | 87.30 ± 0.20 | kJ/mol | NIST |
| ΔsubH° | 89.76 ± 0.81 | kJ/mol | NIST |
| ΔsubH° | 87.30 ± 0.20 | kJ/mol | NIST |
| ΔsubH° | 89.76 ± 0.81 | kJ/mol | NIST |
| ΔvapH° | 64.97 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [9.07; 9.19] | eV |
|
| IE | 9.07 ± 0.02 | eV | NIST |
| IE | 9.19 | eV | NIST |
| log10WS | 0.25 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.677 | Crippen Calculated Property | |
| McVol | 96.090 | ml/mol | McGowan Calculated Property |
| Pc | 4621.41 | kPa | Joback Calculated Property |
| Inp | [215.49; 1266.00] |
|
|
| Inp | 1244.00 | NIST | |
| Inp | 1252.90 | NIST | |
| Inp | 1244.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 1255.00 | NIST | |
| Inp | 1266.00 | NIST | |
| Inp | 215.49 | NIST | |
| Inp | 217.00 | NIST | |
| Inp | 215.49 | NIST | |
| Inp | 1252.90 | NIST | |
| S°solid,1 bar | [168.40; 173.21] | J/mol×K |
|
| S°solid,1 bar | 173.21 | J/mol×K | NIST |
| S°solid,1 bar | 168.40 | J/mol×K | NIST |
| S°solid,1 bar | 168.60 | J/mol×K | NIST |
| S°solid,1 bar | 168.60 | J/mol×K | NIST |
| Tboil | 528.05 | K | Relay (1.0) Calculated Property |
| Tc | 801.00 | K | Critical temperatures and pressures of caprolactam, dimethyl sulfoxide, 1,4-dimethylpiperazine, and 2,6-dimethylpiperazine |
| Tfus | [342.20; 342.35] | K |
|
| Tfus | 342.21 | K | Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes |
| Tfus | 342.30 ± 0.50 | K | NIST |
| Tfus | 342.25 | K | NIST |
| Tfus | 342.35 ± 0.03 | K | NIST |
| Tfus | 342.20 ± 0.50 | K | NIST |
| Ttriple | [342.30; 342.31] | K |
|
| Ttriple | 342.31 ± 0.01 | K | NIST |
| Ttriple | 342.30 ± 0.01 | K | NIST |
| Ttriple | 342.31 ± 0.01 | K | NIST |
| Ttriple | 342.30 ± 0.01 | K | NIST |
Cheméo can also estimate Critical Volume for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 410.20 | K | 1.30 | NIST |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [110.97; 339.42] | 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 | -2.58800e+01 | |||
| Coefficient B | 5.31100e-01 | |||
| Coefficient C | -8.80000e-05 | |||
| Coefficient D | -7.78000e-08 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 273.00 | |||
| Temperature range, max. | 1000.00 | |||
| Cp,gas | 110.97 | J/mol×K | 273.00 | Calculated Property |
| Cp,gas | 147.55 | J/mol×K | 353.78 | Calculated Property |
| Cp,gas | 181.91 | J/mol×K | 434.56 | Calculated Property |
| Cp,gas | 213.80 | J/mol×K | 515.33 | Calculated Property |
| Cp,gas | 242.96 | J/mol×K | 596.11 | Calculated Property |
| Cp,gas | 269.17 | J/mol×K | 676.89 | Calculated Property |
| Cp,gas | 292.16 | J/mol×K | 757.67 | Calculated Property |
| Cp,gas | 311.70 | J/mol×K | 838.44 | Calculated Property |
| Cp,gas | 327.53 | J/mol×K | 919.22 | Calculated Property |
| Cp,gas | 339.42 | J/mol×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.03; 4814.78] | kPa | [342.36; 806.00] |
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 | 1.13763e+02 | |||
| Coefficient B | -1.26926e+04 | |||
| Coefficient C | -1.38483e+01 | |||
| Coefficient D | 4.82981e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 342.36 | |||
| Temperature range, max. | 806.00 | |||
| Pvap | 0.03 | kPa | 342.36 | Calculated Property |
| Pvap | 0.62 | kPa | 393.88 | Calculated Property |
| Pvap | 5.83 | kPa | 445.39 | Calculated Property |
| Pvap | 31.09 | kPa | 496.91 | Calculated Property |
| Pvap | 113.34 | kPa | 548.42 | Calculated Property |
| Pvap | 317.39 | kPa | 599.94 | Calculated Property |
| Pvap | 737.81 | kPa | 651.45 | Calculated Property |
| Pvap | 1501.98 | kPa | 702.97 | Calculated Property |
| Pvap | 2781.13 | kPa | 754.48 | Calculated Property |
| Pvap | 4814.78 | kPa | 806.00 | Calculated Property |
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