- InChI
- InChI=1S/NO2/c2-1-3
- InChI Key
- JCXJVPUVTGWSNB-UHFFFAOYSA-N
- Formula
- NO2
- SMILES
- [O]N=O
- Molecular Weight1
- 46.01
- CAS
- 10102-44-0
- Other Names
-
- Azote
- Nitrito
- Nitro
- Nitrogen dioxide (NO2)
- Nitrogen oxide
- Nitrogen peroxide
- Rcra waste number P078
- Stickstoffdioxid
- Stikstofdioxyde
- nitrogen oxide (NO2)
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- BasG : Gas basicity (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- 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).
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- ρc : Critical density (kg/m3).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.8340; 0.8511] |
|
|
| ω | 0.8511 | ChemSep v8.3 pure component data | |
| ω | 0.8340 | KDB | |
| PAff | 591.00 | kJ/mol | NIST |
| BasG | 560.30 | kJ/mol | NIST |
| μ | [0.31; 0.40] | debye |
|
| μ | 0.31 | debye | ChemSep v8.3 pure component data |
| μ | 0.40 | debye | KDB |
| EA | [1.80; 3.99] | eV |
|
| EA | 2.27 ± 0.01 | eV | NIST |
| EA | 2.30 ± 0.10 | eV | NIST |
| EA | 2.27 ± 0.03 | eV | NIST |
| EA | 2.36 ± 0.10 | eV | NIST |
| EA | 2.35 ± 0.10 | eV | NIST |
| EA | 2.40 ± 0.10 | eV | NIST |
| EA | 2.28 ± 0.10 | eV | NIST |
| EA | 2.38 ± 0.06 | eV | NIST |
| EA | 2.30 ± 0.15 | eV | NIST |
| EA | 2.11 ± 0.18 | eV | NIST |
| EA | 2.80 ± 0.05 | eV | NIST |
| EA | 1.80 ± 0.05 | eV | NIST |
| EA | 2.60 | eV | NIST |
| EA | 1.80 ± 0.20 | eV | NIST |
| EA | 2.10 | eV | NIST |
| EA | 2.50 ± 0.05 | eV | NIST |
| EA | 2.50 ± 0.10 | eV | NIST |
| EA | 2.50 ± 0.10 | eV | NIST |
| EA | 2.04 | eV | NIST |
| EA | 2.07 ± 0.24 | eV | NIST |
| EA | 3.10 ± 0.05 | eV | NIST |
| EA | Outlier 3.90 ± 0.20 | eV | NIST |
| EA | Outlier 3.82 | eV | NIST |
| EA | Outlier 3.99 | eV | NIST |
| ΔfG° | [51.33; 52.00] | kJ/mol |
|
| ΔfG° | 51.33 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | 52.00 | kJ/mol | KDB |
| ΔfH°gas | [33.18; 33.87] | kJ/mol |
|
| ΔfH°gas | 33.18 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | 33.87 | kJ/mol | KDB |
| ΔfusH° | 8.80 | kJ/mol | Joback Calculated Property |
| IE | [9.59; 11.23] | eV |
|
| IE | 9.59 ± 0.00 | eV | NIST |
| IE | 9.60 ± 0.03 | eV | NIST |
| IE | 9.59 ± 0.00 | eV | NIST |
| IE | 11.23 | eV | NIST |
| IE | 10.40 ± 0.30 | eV | NIST |
| IE | 9.62 ± 0.01 | eV | NIST |
| IE | 9.75 ± 0.01 | eV | NIST |
| IE | 11.23 | eV | NIST |
| logPoct/wat | 0.098 | Crippen Calculated Property | |
| McVol | 26.130 | ml/mol | McGowan Calculated Property |
| Pc | [10100.00; 10132.50] | kPa |
|
| Pc | 10132.50 | kPa | ChemSep v8.3 pure component data |
| Pc | 10132.00 | kPa | Air Liquide Gas Encyclopedia |
| Pc | 10100.00 | kPa | KDB |
| Ptriple | [18.70; 18.73] | kPa |
|
| Ptriple | 18.73 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 18.70 | kPa | Air Liquide Gas Encyclopedia |
| ρc | 557.72 | kg/m3 | Air Liquide Gas Encyclopedia |
| Tboil | [294.15; 295.08] | K |
|
| Tboil | 294.15 | K | ChemSep v8.3 pure component data |
| Tboil | 294.15 | K | Air Liquide Gas Encyclopedia |
| Tboil | 294.30 | K | KDB |
| Tboil | 295.08 ± 0.50 | K | NIST |
| Tc | [431.00; 431.15] | K |
|
| Tc | 431.15 | K | ChemSep v8.3 pure component data |
| Tc | 431.15 | K | Air Liquide Gas Encyclopedia |
| Tc | 431.00 | K | KDB |
| Tfus | [261.90; 261.95] | K |
|
| Tfus | 261.90 | K | ChemSep v8.3 pure component data |
| Tfus | 261.95 | K | Air Liquide Gas Encyclopedia |
| Tfus | 261.90 | K | KDB |
| Ttriple | [261.90; 261.90] | K |
|
| Ttriple | 261.90 | K | ChemSep v8.3 pure component data |
| Ttriple | 261.90 | K | Air Liquide Gas Encyclopedia |
| UQi | 1.13 | ChemSep v8.3 pure component data | |
| URi | 1.05 | ChemSep v8.3 pure component data | |
| Vc | [0.082; 0.168] | m3/kmol |
|
| Vc | 0.082 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.168 | m3/kmol | KDB |
| Zc | [0.2330000; 0.4729330] |
|
|
| Zc | 0.2330000 | ChemSep v8.3 pure component data | |
| Zc | 0.4729330 | KDB | |
| Zra | 0.24 | 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.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔfusH | 14.65 | kJ/mol | 261.95 | Air Liquide Gas Encyclopedia |
| ΔvapH | 38.12 | kJ/mol | 294.15 | Air Liquide Gas Encyclopedia |
| ρg | 3.40 | kg/m3 | 294.15 | Air Liquide Gas Encyclopedia |
| ρl | [1447.58; 1450.00] | kg/m3 | [293.00; 294.15] |
|
| ρl | 1450.00 | kg/m3 | 293.00 | KDB |
| ρl | 1447.58 | kg/m3 | 294.15 | Air Liquide Gas Encyclopedia |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [32.96; 56.49] | J/mol×K | [50.00; 1500.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 3.29630e+01 | |||
| Coefficient B | -5.78775e+02 | |||
| Coefficient C | 3.54145e+00 | |||
| Coefficient D | 7.93322e-05 | |||
| Coefficient E | -5.18104e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 50.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 32.96 | J/mol×K | 50.00 | Calculated Property |
| Cp,gas | 35.22 | J/mol×K | 211.11 | Calculated Property |
| Cp,gas | 40.42 | J/mol×K | 372.22 | Calculated Property |
| Cp,gas | 44.95 | J/mol×K | 533.33 | Calculated Property |
| Cp,gas | 48.42 | J/mol×K | 694.44 | Calculated Property |
| Cp,gas | 51.04 | J/mol×K | 855.56 | Calculated Property |
| Cp,gas | 53.03 | J/mol×K | 1016.67 | Calculated Property |
| Cp,gas | 54.54 | J/mol×K | 1177.78 | Calculated Property |
| Cp,gas | 55.67 | J/mol×K | 1338.89 | Calculated Property |
| Cp,gas | 56.49 | J/mol×K | 1500.00 | Calculated Property |
| Cp,gas | [36.97; 53.76] | J/mol×K | [298.00; 1200.00] |
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 | 1.61086e+01 | |||
| Coefficient B | 7.58953e+01 | |||
| Coefficient C | -5.43874e+01 | |||
| Coefficient D | 1.43078e+01 | |||
| Coefficient E | 2.39423e-01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=26.17464, G=240.5386, H=33.09502; Data last reviewed in September, 1964 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 36.97 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 40.12 | J/mol×K | 398.22 | Calculated Property |
| Cp,gas | 43.16 | J/mol×K | 498.44 | Calculated Property |
| Cp,gas | 45.79 | J/mol×K | 598.67 | Calculated Property |
| Cp,gas | 47.96 | J/mol×K | 698.89 | Calculated Property |
| Cp,gas | 49.70 | J/mol×K | 799.11 | Calculated Property |
| Cp,gas | 51.08 | J/mol×K | 899.33 | Calculated Property |
| Cp,gas | 52.16 | J/mol×K | 999.56 | Calculated Property |
| Cp,gas | 53.02 | J/mol×K | 1099.78 | Calculated Property |
| Cp,gas | 53.76 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | [53.73; 58.00] | J/mol×K | [1200.00; 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 | 5.68254e+01 | |||
| Coefficient B | 7.38053e-01 | |||
| Coefficient C | -1.44721e-01 | |||
| Coefficient D | 9.77700e-03 | |||
| Coefficient E | -5.45991e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=2.846456, G=290.5056, H=33.09502; Data last reviewed in September, 1964 | |||
| Temperature range, min. | 1200.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 53.73 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 55.90 | J/mol×K | 1733.33 | Calculated Property |
| Cp,gas | 56.81 | J/mol×K | 2266.67 | Calculated Property |
| Cp,gas | 57.28 | J/mol×K | 2800.00 | Calculated Property |
| Cp,gas | 57.55 | J/mol×K | 3333.33 | Calculated Property |
| Cp,gas | 57.72 | J/mol×K | 3866.67 | Calculated Property |
| Cp,gas | 57.82 | J/mol×K | 4400.00 | Calculated Property |
| Cp,gas | 57.89 | J/mol×K | 4933.33 | Calculated Property |
| Cp,gas | 57.95 | J/mol×K | 5466.67 | Calculated Property |
| Cp,gas | 58.00 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [136.33; 158.73] | J/mol×K | [261.00; 400.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 7.74350e+01 | |||
| Coefficient B | 4.32690e+02 | |||
| Coefficient C | -1.53406e+00 | |||
| Coefficient D | 2.08040e-02 | |||
| Coefficient E | -2.16950e-05 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 261.00 | |||
| Temperature range, max. | 400.00 | |||
| Cp,liquid | 136.33 | J/mol×K | 261.00 | Calculated Property |
| Cp,liquid | 139.26 | J/mol×K | 276.44 | Calculated Property |
| Cp,liquid | 142.31 | J/mol×K | 291.89 | Calculated Property |
| Cp,liquid | 145.36 | J/mol×K | 307.33 | Calculated Property |
| Cp,liquid | 148.33 | J/mol×K | 322.78 | Calculated Property |
| Cp,liquid | 151.12 | J/mol×K | 338.22 | Calculated Property |
| Cp,liquid | 153.64 | J/mol×K | 353.67 | Calculated Property |
| Cp,liquid | 155.80 | J/mol×K | 369.11 | Calculated Property |
| Cp,liquid | 157.52 | J/mol×K | 384.56 | Calculated Property |
| Cp,liquid | 158.73 | J/mol×K | 400.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0007090; 0.0000769] | Pa×s | [253.15; 400.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | -3.11490e+02 | |||
| Coefficient B | 1.00410e+04 | |||
| Coefficient C | 4.90270e+01 | |||
| Coefficient D | -1.05180e-04 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 253.15 | |||
| Temperature range, max. | 400.00 | |||
| η | 0.0007090 | Pa×s | 253.15 | Calculated Property |
| η | 0.0005598 | Pa×s | 269.47 | Calculated Property |
| η | 0.0004592 | Pa×s | 285.78 | Calculated Property |
| η | 0.0003818 | Pa×s | 302.10 | Calculated Property |
| η | 0.0003160 | Pa×s | 318.42 | Calculated Property |
| η | 0.0002567 | Pa×s | 334.73 | Calculated Property |
| η | 0.0002024 | Pa×s | 351.05 | Calculated Property |
| η | 0.0001536 | Pa×s | 367.37 | Calculated Property |
| η | 0.0001114 | Pa×s | 383.68 | Calculated Property |
| η | 0.0000769 | Pa×s | 400.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [38.32; 0.00] | kJ/mol | [291.15; 431.15] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 5.37000e+01 | |||
| Coefficient B | 3.00000e-01 | |||
| Coefficient C | 0.00000e+00 | |||
| Coefficient D | 0.00000e+00 | |||
| Coefficient E | 0.00000e+00 | |||
| Critical temperature, Tc (K) | 4.31150e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 291.15 | |||
| Temperature range, max. | 431.15 | |||
| ΔvapH | 38.32 | kJ/mol | 291.15 | Calculated Property |
| ΔvapH | 36.99 | kJ/mol | 306.71 | Calculated Property |
| ΔvapH | 35.54 | kJ/mol | 322.26 | Calculated Property |
| ΔvapH | 33.93 | kJ/mol | 337.82 | Calculated Property |
| ΔvapH | 32.12 | kJ/mol | 353.37 | Calculated Property |
| ΔvapH | 30.04 | kJ/mol | 368.93 | Calculated Property |
| ΔvapH | 27.56 | kJ/mol | 384.48 | Calculated Property |
| ΔvapH | 24.40 | kJ/mol | 400.04 | Calculated Property |
| ΔvapH | 19.82 | kJ/mol | 415.59 | Calculated Property |
| ΔvapH | 0.00 | kJ/mol | 431.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [18.74; 10124.77] | kPa | [261.95; 431.35] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 2.04197e+01 | |||
| Coefficient B | -5.27208e+03 | |||
| Coefficient C | 3.95000e+01 | |||
| Temperature range, min. | 261.95 | |||
| Temperature range, max. | 431.35 | |||
| Pvap | 18.74 | kPa | 261.95 | Calculated Property |
| Pvap | 52.38 | kPa | 280.77 | Calculated Property |
| Pvap | 130.60 | kPa | 299.59 | Calculated Property |
| Pvap | 295.83 | kPa | 318.42 | Calculated Property |
| Pvap | 617.51 | kPa | 337.24 | Calculated Property |
| Pvap | 1201.80 | kPa | 356.06 | Calculated Property |
| Pvap | 2201.67 | kPa | 374.88 | Calculated Property |
| Pvap | 3826.69 | kPa | 393.71 | Calculated Property |
| Pvap | 6351.87 | kPa | 412.53 | Calculated Property |
| Pvap | 10124.77 | kPa | 431.35 | Calculated Property |
| Pvap | [11.36; 10121.54] | kPa | [252.77; 431.37] |
ChemSep v8.3 pure component data
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.14962e+01 | |||
| Coefficient B | -3.50860e+03 | |||
| Coefficient C | 8.12550e-01 | |||
| Coefficient D | 4.99830e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 252.77 | |||
| Temperature range, max. | 431.37 | |||
| Pvap | 11.36 | kPa | 252.77 | Calculated Property |
| Pvap | 34.97 | kPa | 272.61 | Calculated Property |
| Pvap | 93.76 | kPa | 292.46 | Calculated Property |
| Pvap | 225.07 | kPa | 312.30 | Calculated Property |
| Pvap | 493.55 | kPa | 332.15 | Calculated Property |
| Pvap | 1004.42 | kPa | 351.99 | Calculated Property |
| Pvap | 1920.80 | kPa | 371.84 | Calculated Property |
| Pvap | 3486.12 | kPa | 391.68 | Calculated Property |
| Pvap | 6053.14 | kPa | 411.53 | Calculated Property |
| Pvap | 10121.54 | kPa | 431.37 | Calculated Property |
| Pvap | [0.11; 103.91] | kPa | [217.60; 294.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.23245e+01 | |||
| Coefficient B | -1.24486e+03 | |||
| Coefficient C | -1.31930e+02 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 217.60 | |||
| Temperature range, max. | 294.00 | |||
| Pvap | 0.11 | kPa | 217.60 | Calculated Property |
| Pvap | 0.41 | kPa | 226.09 | Calculated Property |
| Pvap | 1.22 | kPa | 234.58 | Calculated Property |
| Pvap | 3.08 | kPa | 243.07 | Calculated Property |
| Pvap | 6.81 | kPa | 251.56 | Calculated Property |
| Pvap | 13.57 | kPa | 260.04 | Calculated Property |
| Pvap | 24.82 | kPa | 268.53 | Calculated Property |
| Pvap | 42.30 | kPa | 277.02 | Calculated Property |
| Pvap | 67.97 | kPa | 285.51 | Calculated Property |
| Pvap | 103.91 | kPa | 294.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1519.36; 538.42] | kg/m3 | [261.90; 431.37] |
ChemSep v8.3 pure component data
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 1.02036e+02 | |||
| Coefficient B | 2.29940e-01 | |||
| Coefficient C | 4.31380e+02 | |||
| Coefficient D | 1.90060e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 261.90 | |||
| Temperature range, max. | 431.37 | |||
| ρl | 1519.36 | kg/m3 | 261.90 | Calculated Property |
| ρl | 1478.53 | kg/m3 | 280.73 | Calculated Property |
| ρl | 1434.60 | kg/m3 | 299.56 | Calculated Property |
| ρl | 1386.82 | kg/m3 | 318.39 | Calculated Property |
| ρl | 1334.03 | kg/m3 | 337.22 | Calculated Property |
| ρl | 1274.44 | kg/m3 | 356.05 | Calculated Property |
| ρl | 1204.88 | kg/m3 | 374.88 | Calculated Property |
| ρl | 1118.86 | kg/m3 | 393.71 | Calculated Property |
| ρl | 998.20 | kg/m3 | 412.54 | Calculated Property |
| ρl | 538.42 | kg/m3 | 431.37 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.03; 0.00] | N/m | [261.90; 422.24] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -9.33460e-02 | |||
| Coefficient B | -8.00910e+01 | |||
| Coefficient C | -1.09500e+00 | |||
| Coefficient D | -2.60370e-03 | |||
| Coefficient E | 2.07710e-07 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 261.90 | |||
| Temperature range, max. | 422.24 | |||
| γ | 0.03 | N/m | 261.90 | Calculated Property |
| γ | 0.03 | N/m | 279.72 | Calculated Property |
| γ | 0.03 | N/m | 297.53 | Calculated Property |
| γ | 0.02 | N/m | 315.35 | Calculated Property |
| γ | 0.02 | N/m | 333.16 | Calculated Property |
| γ | 0.02 | N/m | 350.98 | Calculated Property |
| γ | 0.01 | N/m | 368.79 | Calculated Property |
| γ | 0.01 | N/m | 386.61 | Calculated Property |
| γ | 0.01 | N/m | 404.42 | Calculated Property |
| γ | 0.00 | N/m | 422.24 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.04; 0.09] | W/m×K | [420.00; 1000.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 7.08510e-02 | |||
| Coefficient B | -2.14300e-01 | |||
| Coefficient C | -1.25800e+03 | |||
| Coefficient D | 4.29500e+05 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 420.00 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.04 | W/m×K | 420.00 | Calculated Property |
| λ | 0.08 | W/m×K | 484.44 | Calculated Property |
| λ | 0.14 | W/m×K | 548.89 | Calculated Property |
| λ | 0.20 | W/m×K | 613.33 | Calculated Property |
| λ | 0.22 | W/m×K | 677.78 | Calculated Property |
| λ | 0.20 | W/m×K | 742.22 | Calculated Property |
| λ | 0.17 | W/m×K | 806.67 | Calculated Property |
| λ | 0.14 | W/m×K | 871.11 | Calculated Property |
| λ | 0.11 | W/m×K | 935.56 | Calculated Property |
| λ | 0.09 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.16; 0.12] | W/m×K | [270.00; 350.00] |
ChemSep v8.3 pure component data
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 1.16110e-01 | |||
| Coefficient B | 1.27610e+05 | |||
| Coefficient C | -1.40910e+03 | |||
| Coefficient D | 5.17770e+00 | |||
| Coefficient E | -6.37380e-03 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 270.00 | |||
| Temperature range, max. | 350.00 | |||
| λ | 0.16 | W/m×K | 270.00 | Calculated Property |
| λ | 0.15 | W/m×K | 278.89 | Calculated Property |
| λ | 0.15 | W/m×K | 287.78 | Calculated Property |
| λ | 0.14 | W/m×K | 296.67 | Calculated Property |
| λ | 0.13 | W/m×K | 305.56 | Calculated Property |
| λ | 0.12 | W/m×K | 314.44 | Calculated Property |
| λ | 0.12 | W/m×K | 323.33 | Calculated Property |
| λ | 0.12 | W/m×K | 332.22 | Calculated Property |
| λ | 0.12 | W/m×K | 341.11 | Calculated Property |
| λ | 0.12 | W/m×K | 350.00 | Calculated Property |
Similar Compounds
Find more compounds similar to Nitrogen dioxide.
Mixtures
Sources
- Air Liquide Gas Encyclopedia
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Crippen Method
- Crippen Method
- Experimental study of high pressure phase equilibrium of (CO2 + NO2/N2O4) mixtures
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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