- InChI
- InChI=1S/F3NO/c1-4(2,3)5
- InChI Key
- UDOZVPVDQKQJAP-UHFFFAOYSA-N
- Formula
- F3NO
- SMILES
- [O-][N+](F)(F)F
- Molecular Weight1
- 87.00
- CAS
- 13847-65-9
- Other Names
-
- AMOX
- NF3O
- NOF3
- Nitrogen Fluoride oxide (F3NO)
- Nitrogen fluoride oxide (NF3O)
- Nitrogen trifluoride oxide
- Trifluoramine oxide
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Tc : Critical Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| IE | [13.26; 13.36] | eV |
|
| IE | 13.31 ± 0.06 | eV | NIST |
| IE | 13.36 ± 0.01 | eV | NIST |
| IE | 13.26 ± 0.01 | eV | NIST |
| logPoct/wat | 0.955 | Crippen Calculated Property | |
| McVol | 32.020 | ml/mol | McGowan Calculated Property |
| Tc | 302.60 | K | Mathews (1972), critical constants of inorganic substances Compiled value |
| Vc | 0.169 | m3/kmol | Mathews (1972), critical constants of inorganic substances Compiled value |
Cheméo can also estimate Normal Boiling Point Temperature, Normal melting (fusion) point, Critical Pressure, Enthalpy of formation at standard conditions, Enthalpy of vaporization at standard conditions, Standard Gibbs free energy of formation, Acentric Factor, 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.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | 16.10 | kJ/mol | 153.50 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [67.82; 101.69] | J/mol×K | [298.00; 1100.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 4.66273e+01 | |||
| Coefficient B | 1.33481e+02 | |||
| Coefficient C | -1.14593e+02 | |||
| Coefficient D | 3.57434e+01 | |||
| Coefficient E | -8.30984e-01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-184.8587, G=295.2151, H=-163.1760; Data last reviewed in June, 1970 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 1100.00 | |||
| Cp,gas | 67.82 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 77.66 | J/mol×K | 387.11 | Calculated Property |
| Cp,gas | 84.40 | J/mol×K | 476.22 | Calculated Property |
| Cp,gas | 89.32 | J/mol×K | 565.33 | Calculated Property |
| Cp,gas | 92.98 | J/mol×K | 654.44 | Calculated Property |
| Cp,gas | 95.71 | J/mol×K | 743.56 | Calculated Property |
| Cp,gas | 97.76 | J/mol×K | 832.67 | Calculated Property |
| Cp,gas | 99.32 | J/mol×K | 921.78 | Calculated Property |
| Cp,gas | 100.57 | J/mol×K | 1010.89 | Calculated Property |
| Cp,gas | 101.69 | J/mol×K | 1100.00 | Calculated Property |
| Cp,gas | [101.63; 107.86] | J/mol×K | [1100.00; 6000.00] |
NIST
|
| Equation | Y = A + B·t + C·t² + D·t³ + E/t², t = T/1000 Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 1.06628e+02 | |||
| Coefficient B | 8.09993e-01 | |||
| Coefficient C | -1.63066e-01 | |||
| Coefficient D | 1.12490e-02 | |||
| Coefficient E | -6.90803e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-213.8070, G=379.5457, H=-163.1760; Data last reviewed in June, 1970 | |||
| Temperature range, min. | 1100.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 101.63 | J/mol×K | 1100.00 | Calculated Property |
| Cp,gas | 105.01 | J/mol×K | 1644.44 | Calculated Property |
| Cp,gas | 106.30 | J/mol×K | 2188.89 | Calculated Property |
| Cp,gas | 106.93 | J/mol×K | 2733.33 | Calculated Property |
| Cp,gas | 107.28 | J/mol×K | 3277.78 | Calculated Property |
| Cp,gas | 107.50 | J/mol×K | 3822.22 | Calculated Property |
| Cp,gas | 107.63 | J/mol×K | 4366.67 | Calculated Property |
| Cp,gas | 107.72 | J/mol×K | 4911.11 | Calculated Property |
| Cp,gas | 107.79 | J/mol×K | 5455.56 | Calculated Property |
| Cp,gas | 107.86 | J/mol×K | 6000.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Trifluoroamine oxide.
Sources
- Mathews (1972), critical constants of inorganic substances ChEDL chemicals 1.5.2, from Mathews, J. F. Critical Constants of Inorganic Substances. Chem. Rev. 1972, 72, 71-100.
- Cheméo Relay (1.0, beta) Beta: served but experimental, data-limited and below our cross-validation release bar; the Joback value is recommended where available.
- Crippen Method
- Crippen Method
- McGowan Method
- NIST Webbook
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