| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5880 | KDB | |
| PAff | [526.10; 531.80] | kJ/mol |
|
| PAff | 531.80 | kJ/mol | NIST |
| PAff | 526.10 ± 1.30 | kJ/mol | NIST |
| BasG | 505.30 | kJ/mol | NIST |
| μ | 0.20 | debye | KDB |
| ΔfG° | 86.75 | kJ/mol | KDB |
| ΔfH°gas | 90.43 | kJ/mol | KDB |
| IE | [9.20; 9.54] | eV |
|
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.23 | eV | NIST |
| IE | 9.20 ± 0.10 | eV | NIST |
| IE | Outlier 9.54 | eV | NIST |
| IE | 9.26 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.27 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.27 | eV | NIST |
| IE | 9.25 ± 0.02 | eV | NIST |
| IE | 9.25 ± 0.15 | eV | NIST |
| IE | 9.27 | eV | NIST |
| IE | 9.26 ± 0.00 | eV | NIST |
| IE | 9.27 ± 0.05 | eV | NIST |
| IE | 9.28 ± 0.03 | eV | NIST |
| IE | 9.27 ± 0.01 | eV | NIST |
| IE | 9.25 ± 0.01 | eV | NIST |
| IE | 9.27 ± 0.01 | eV | NIST |
| IE | 9.25 ± 0.02 | eV | NIST |
| IE | 9.26 | eV | NIST |
| logPoct/wat | -0.447 | Crippen Calculated Property | |
| McVol | 20.260 | ml/mol | McGowan Calculated Property |
| Pc | 6480.00 | kPa | KDB |
| Ptriple | 21.92 | kPa | KDB |
| Tboil | 121.41 | K | KDB |
| Tc | 180.00 | K | KDB |
| Tfus | 109.50 | K | KDB |
| Ttriple | 109.54 | K | KDB |
| Vc | 0.058 | m3/kmol | KDB |
| Zc | 0.2511270 | KDB | |
| Zra | 0.27 | KDB |
Cheméo can also estimate Enthalpy of vaporization at standard conditions, Log10 of Water solubility in mol/l for this compound, but they fall outside the models' validated range, so they are not shown here. Open the prediction tool to compute them on demand.
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 13.80 | kJ/mol | 212.00 | NIST |
| Pvap | [188.30; 987.80] | kPa | [127.32; 146.22] | |
| Pvap | 188.30 | kPa | 127.32 | Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air |
| Pvap | 410.90 | kPa | 135.80 | Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air |
| Pvap | 987.80 | kPa | 146.22 | Phase Equilibrium of Three Binary Mixtures Containing NO and Components Present in Ambient Air |
| ρl | 1280.00 | kg/m3 | 121.00 | KDB |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [21.96; 6493.35] | kPa | [109.50; 180.15] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.57218e+01 | |||
| Coefficient B | -1.08919e+03 | |||
| Coefficient C | -2.32800e+01 | |||
| Temperature range, min. | 109.50 | |||
| Temperature range, max. | 180.15 | |||
| Pvap | 21.96 | kPa | 109.50 | Calculated Property |
| Pvap | 63.01 | kPa | 117.35 | Calculated Property |
| Pvap | 153.71 | kPa | 125.20 | Calculated Property |
| Pvap | 330.08 | kPa | 133.05 | Calculated Property |
| Pvap | 640.05 | kPa | 140.90 | Calculated Property |
| Pvap | 1142.43 | kPa | 148.75 | Calculated Property |
| Pvap | 1904.65 | kPa | 156.60 | Calculated Property |
| Pvap | 2999.94 | kPa | 164.45 | Calculated Property |
| Pvap | 4504.26 | kPa | 172.30 | Calculated Property |
| Pvap | 6493.35 | kPa | 180.15 | Calculated Property |
Find more compounds similar to Nitric oxide.
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