| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.4462 | Relay (1.0) Calculated Property | |
| PAff | 967.00 | kJ/mol | NIST |
| BasG | 909.50 | kJ/mol | NIST |
| ΔcH°liquid | -7061.80 ± 7.50 | kJ/mol | NIST |
| ΔcH°solid | -7071.00 ± 4.90 | kJ/mol | NIST |
| ΔfG° | -579.60 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -980.54 | kJ/mol | Relay (1.0) Calculated Property |
| ΔfH°solid | -1081.10 ± 2.80 | kJ/mol | NIST |
| ΔfusH° | 35.50 | kJ/mol | The Water 18-Crown-6 System: Experimental Investigation and Thermodynamic Modeling |
| ΔsubH° | 119.10 ± 6.70 | kJ/mol | NIST |
| ΔvapH° | 86.10 ± 6.70 | kJ/mol | NIST |
| IE | [8.90; 9.70] | eV |
|
| IE | 8.90 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.70 | eV | NIST |
| log10WS | -0.13 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.100 | Crippen Calculated Property | |
| McVol | 204.300 | ml/mol | McGowan Calculated Property |
| Pc | 2811.36 | kPa | Joback Calculated Property |
| I | [2504.00; 2504.00] |
|
|
| I | 2504.00 | NIST | |
| I | 2504.00 | NIST | |
| Tboil | 637.57 | K | Relay (1.0) Calculated Property |
| Tc | 815.45 | K | Relay (1.0) Calculated Property |
| Tfus | [310.00; 316.50] | K |
|
| Tfus | 312.25 | K | Structure and properties of congruent melting 18-crown-6 crystalline hydrates |
| Tfus | 312.32 | K | Enthalpies of fusion, vaporisation and sublimation of crown ethers determined by thermogravimetry and differential scanning calorimetry |
| Tfus | 316.50 | K | Static Dielectric Permittivity of Homologous Series of Liquid Cyclic Ethers, 3n-Crown-n, n = 4 to 6 |
| Tfus | 310.00 ± 1.00 | K | NIST |
| Vc | 0.695 | m3/kmol | Relay (1.0) Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [637.05; 751.60] | J/mol×K | [711.12; 981.43] | |
| Cp,gas | 637.05 | J/mol×K | 711.12 | Joback Calculated Property |
| Cp,gas | 663.41 | J/mol×K | 756.17 | Joback Calculated Property |
| Cp,gas | 687.05 | J/mol×K | 801.22 | Joback Calculated Property |
| Cp,gas | 707.82 | J/mol×K | 846.28 | Joback Calculated Property |
| Cp,gas | 725.59 | J/mol×K | 891.33 | Joback Calculated Property |
| Cp,gas | 740.23 | J/mol×K | 936.38 | Joback Calculated Property |
| Cp,gas | 751.60 | J/mol×K | 981.43 | Joback Calculated Property |
| η | [0.0000026; 0.0089867] | Pa×s | [353.80; 711.12] | |
| η | 0.0089867 | Pa×s | 353.80 | Joback Calculated Property |
| η | 0.0008700 | Pa×s | 413.35 | Joback Calculated Property |
| η | 0.0001517 | Pa×s | 472.91 | Joback Calculated Property |
| η | 0.0000391 | Pa×s | 532.46 | Joback Calculated Property |
| η | 0.0000132 | Pa×s | 592.01 | Joback Calculated Property |
| η | 0.0000055 | Pa×s | 651.57 | Joback Calculated Property |
| η | 0.0000026 | Pa×s | 711.12 | Joback Calculated Property |
| ΔfusH | 34.00 | kJ/mol | 312.20 | NIST |
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 391.50 ± 0.50 | K | 0.01 | NIST |
| Tfus | 311.76 | K | 101.30 | (Solid + liquid) phase equilibria of binary mixtures containing N-methyl-2-pyrrolidinone and ethers at atmospheric pressure |
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