- InChI
- InChI=1S/O3/c1-3-2
- InChI Key
- CBENFWSGALASAD-UHFFFAOYSA-N
- Formula
- O3
- SMILES
- O=[O+][O-]
- Molecular Weight1
- 48.00
- CAS
- 10028-15-6
- Other Names
-
- TRIATOMIC OXYGEN
- 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 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).
- 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 | [0.1947; 0.2240] |
|
|
| ω | 0.2240 | ChemSep v8.3 pure component data | |
| ω | 0.1947 | KDB | |
| PAff | 625.50 | kJ/mol | NIST |
| BasG | 595.90 | kJ/mol | NIST |
| μ | [0.54; 0.60] | debye |
|
| μ | 0.54 | debye | ChemSep v8.3 pure component data |
| μ | 0.60 | debye | KDB |
| EA | [1.82; 2.14] | eV |
|
| EA | 2.10 ± 0.00 | eV | NIST |
| EA | 2.10 ± 0.00 | eV | NIST |
| EA | 2.14 ± 0.15 | eV | NIST |
| EA | 1.91 ± 0.14 | eV | NIST |
| EA | 1.82 | eV | NIST |
| EA | 1.96 | eV | NIST |
| ΔfG° | [162.90; 163.16] | kJ/mol |
|
| ΔfG° | 163.16 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | 162.90 | kJ/mol | KDB |
| ΔfH°gas | [142.80; 143.10] | kJ/mol |
|
| ΔfH°gas | 143.10 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | 142.80 | kJ/mol | KDB |
| IE | [12.30; 12.89] | eV |
|
| IE | 12.53 ± 0.08 | eV | NIST |
| IE | 12.43 | eV | NIST |
| IE | 12.52 ± 0.00 | eV | NIST |
| IE | 12.50 ± 0.10 | eV | NIST |
| IE | 12.44 ± 0.01 | eV | NIST |
| IE | 12.56 | eV | NIST |
| IE | 12.67 | eV | NIST |
| IE | 12.30 ± 0.10 | eV | NIST |
| IE | 12.89 ± 0.10 | eV | NIST |
| IE | 12.80 ± 0.05 | eV | NIST |
| IE | 12.73 | eV | NIST |
| logPoct/wat | -1.122 | Crippen Calculated Property | |
| McVol | 24.170 | ml/mol | McGowan Calculated Property |
| Pc | [5570.00; 5570.00] | kPa |
|
| Pc | 5570.00 | kPa | ChemSep v8.3 pure component data |
| Pc | 5570.00 | kPa | Air Liquide Gas Encyclopedia |
| Pc | 5570.00 | kPa | KDB |
| Ptriple | [7.35e-04; 7.35e-04] | kPa |
|
| Ptriple | 7.35e-04 | kPa | ChemSep v8.3 pure component data |
| Ptriple | 7.35e-04 | kPa | Air Liquide Gas Encyclopedia |
| ρc | 539.31 | kg/m3 | Air Liquide Gas Encyclopedia |
| Tboil | [161.30; 161.85] | K |
|
| Tboil | 161.80 | K | ChemSep v8.3 pure component data |
| Tboil | 161.85 | K | Air Liquide Gas Encyclopedia |
| Tboil | 161.80 | K | KDB |
| Tboil | 161.30 ± 0.50 | K | NIST |
| Tc | [261.00; 261.15] | K |
|
| Tc | 261.05 | K | ChemSep v8.3 pure component data |
| Tc | 261.00 | K | Air Liquide Gas Encyclopedia |
| Tc | 261.10 | K | KDB |
| Tc | 261.15 ± 1.50 | K | NIST |
| Tc | 261.05 ± 1.00 | K | NIST |
| Tfus | [22.15; 80.70] | K |
|
| Tfus | 22.15 | K | ChemSep v8.3 pure component data |
| Tfus | 80.15 | K | Air Liquide Gas Encyclopedia |
| Tfus | 80.00 | K | KDB |
| Tfus | 80.70 ± 0.50 | K | NIST |
| Ttriple | [80.15; 80.15] | K |
|
| Ttriple | 80.15 | K | ChemSep v8.3 pure component data |
| Ttriple | 80.15 | K | Air Liquide Gas Encyclopedia |
| UQi | 1.27 | ChemSep v8.3 pure component data | |
| URi | 1.10 | ChemSep v8.3 pure component data | |
| Vc | [0.089; 0.089] | m3/kmol |
|
| Vc | 0.089 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.089 | m3/kmol | KDB |
| Zc | [0.2283500; 0.2290000] |
|
|
| Zc | 0.2290000 | ChemSep v8.3 pure component data | |
| Zc | 0.2283500 | KDB | |
| Zra | 0.25 | ChemSep v8.3 pure component data |
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 | 2.00 | kJ/mol | 80.15 | Air Liquide Gas Encyclopedia |
| ΔvapH | 13.85 | kJ/mol | 161.85 | Air Liquide Gas Encyclopedia |
| ρl | [1349.08; 1356.00] | kg/m3 | [161.00; 161.85] |
|
| ρl | 1356.00 | kg/m3 | 161.00 | KDB |
| ρl | 1349.08 | kg/m3 | 161.85 | Air Liquide Gas Encyclopedia |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [32.86; 58.10] | 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 | 3.28596e+01 | |||
| Coefficient B | -6.04741e+02 | |||
| Coefficient C | 4.00431e+00 | |||
| Coefficient D | -2.87995e-04 | |||
| Coefficient E | 2.63241e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 50.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 32.86 | J/mol×K | 50.00 | Calculated Property |
| Cp,gas | 35.80 | J/mol×K | 211.11 | Calculated Property |
| Cp,gas | 42.60 | J/mol×K | 372.22 | Calculated Property |
| Cp,gas | 48.11 | J/mol×K | 533.33 | Calculated Property |
| Cp,gas | 51.89 | J/mol×K | 694.44 | Calculated Property |
| Cp,gas | 54.41 | J/mol×K | 855.56 | Calculated Property |
| Cp,gas | 56.05 | J/mol×K | 1016.67 | Calculated Property |
| Cp,gas | 57.10 | J/mol×K | 1177.78 | Calculated Property |
| Cp,gas | 57.74 | J/mol×K | 1338.89 | Calculated Property |
| Cp,gas | 58.10 | J/mol×K | 1500.00 | Calculated Property |
| Cp,gas | [39.22; 56.20] | 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 | 2.16616e+01 | |||
| Coefficient B | 7.98600e+01 | |||
| Coefficient C | -6.60260e+01 | |||
| Coefficient D | 1.95836e+01 | |||
| Coefficient E | -7.92510e-02 | |||
| Reference | Chase, 1998 | |||
| Comment | F=132.9407, G=243.6406, H=142.6740; Data last reviewed in June, 1961 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 1200.00 | |||
| Cp,gas | 39.22 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 43.73 | J/mol×K | 398.22 | Calculated Property |
| Cp,gas | 47.17 | J/mol×K | 498.44 | Calculated Property |
| Cp,gas | 49.79 | J/mol×K | 598.67 | Calculated Property |
| Cp,gas | 51.75 | J/mol×K | 698.89 | Calculated Property |
| Cp,gas | 53.19 | J/mol×K | 799.11 | Calculated Property |
| Cp,gas | 54.23 | J/mol×K | 899.33 | Calculated Property |
| Cp,gas | 55.00 | J/mol×K | 999.56 | Calculated Property |
| Cp,gas | 55.62 | J/mol×K | 1099.78 | Calculated Property |
| Cp,gas | 56.20 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | [56.17; 61.25] | 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 | 5.78141e+01 | |||
| Coefficient B | 7.30941e-01 | |||
| Coefficient C | -3.92530e-02 | |||
| Coefficient D | 2.61000e-03 | |||
| Coefficient E | -3.56037e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=115.7717, G=294.5607, H=142.6740; Data last reviewed in June, 1961 | |||
| Temperature range, min. | 1200.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 56.17 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 57.79 | J/mol×K | 1733.33 | Calculated Property |
| Cp,gas | 58.61 | J/mol×K | 2266.67 | Calculated Property |
| Cp,gas | 59.16 | J/mol×K | 2800.00 | Calculated Property |
| Cp,gas | 59.59 | J/mol×K | 3333.33 | Calculated Property |
| Cp,gas | 59.97 | J/mol×K | 3866.67 | Calculated Property |
| Cp,gas | 60.31 | J/mol×K | 4400.00 | Calculated Property |
| Cp,gas | 60.63 | J/mol×K | 4933.33 | Calculated Property |
| Cp,gas | 60.94 | J/mol×K | 5466.67 | Calculated Property |
| Cp,gas | 61.25 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [85.35; 102.22] | J/mol×K | [90.00; 150.00] |
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 | 6.45000e+01 | |||
| Coefficient B | -6.02050e+01 | |||
| Coefficient C | 3.07094e+00 | |||
| Coefficient D | 8.04340e-03 | |||
| Coefficient E | -1.09290e-05 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 90.00 | |||
| Temperature range, max. | 150.00 | |||
| Cp,liquid | 85.35 | J/mol×K | 90.00 | Calculated Property |
| Cp,liquid | 87.23 | J/mol×K | 96.67 | Calculated Property |
| Cp,liquid | 89.10 | J/mol×K | 103.33 | Calculated Property |
| Cp,liquid | 90.97 | J/mol×K | 110.00 | Calculated Property |
| Cp,liquid | 92.85 | J/mol×K | 116.67 | Calculated Property |
| Cp,liquid | 94.72 | J/mol×K | 123.33 | Calculated Property |
| Cp,liquid | 96.60 | J/mol×K | 130.00 | Calculated Property |
| Cp,liquid | 98.47 | J/mol×K | 136.67 | Calculated Property |
| Cp,liquid | 100.35 | J/mol×K | 143.33 | Calculated Property |
| Cp,liquid | 102.22 | J/mol×K | 150.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0041022; 0.0001175] | Pa×s | [77.55; 208.80] |
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 | -3.70360e+01 | |||
| Coefficient B | 8.15780e+02 | |||
| Coefficient C | 4.89710e+00 | |||
| Coefficient D | -4.76460e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 77.55 | |||
| Temperature range, max. | 208.80 | |||
| η | 0.0041022 | Pa×s | 77.55 | Calculated Property |
| η | 0.0016038 | Pa×s | 92.13 | Calculated Property |
| η | 0.0008554 | Pa×s | 106.72 | Calculated Property |
| η | 0.0005453 | Pa×s | 121.30 | Calculated Property |
| η | 0.0003864 | Pa×s | 135.88 | Calculated Property |
| η | 0.0002916 | Pa×s | 150.47 | Calculated Property |
| η | 0.0002281 | Pa×s | 165.05 | Calculated Property |
| η | 0.0001820 | Pa×s | 179.63 | Calculated Property |
| η | 0.0001463 | Pa×s | 194.22 | Calculated Property |
| η | 0.0001175 | Pa×s | 208.80 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [16.15; 1.69] | kJ/mol | [80.15; 261.00] |
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 | 1.62540e+01 | |||
| Coefficient B | -7.34470e-02 | |||
| Coefficient C | 1.48230e-01 | |||
| Coefficient D | 6.22250e-01 | |||
| Coefficient E | -4.32770e-01 | |||
| Critical temperature, Tc (K) | 2.61050e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 80.15 | |||
| Temperature range, max. | 261.00 | |||
| ΔvapH | 16.15 | kJ/mol | 80.15 | Calculated Property |
| ΔvapH | 15.86 | kJ/mol | 100.24 | Calculated Property |
| ΔvapH | 15.42 | kJ/mol | 120.34 | Calculated Property |
| ΔvapH | 14.83 | kJ/mol | 140.43 | Calculated Property |
| ΔvapH | 14.05 | kJ/mol | 160.53 | Calculated Property |
| ΔvapH | 13.09 | kJ/mol | 180.62 | Calculated Property |
| ΔvapH | 11.92 | kJ/mol | 200.72 | Calculated Property |
| ΔvapH | 10.47 | kJ/mol | 220.81 | Calculated Property |
| ΔvapH | 8.50 | kJ/mol | 240.91 | Calculated Property |
| ΔvapH | 1.69 | kJ/mol | 261.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [2.79e-04; 5578.47] | kPa | [80.15; 261.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44711e+01 | |||
| Coefficient B | -1.42440e+03 | |||
| Coefficient C | -1.72800e+01 | |||
| Temperature range, min. | 80.15 | |||
| Temperature range, max. | 261.00 | |||
| Pvap | 2.79e-04 | kPa | 80.15 | Calculated Property |
| Pvap | 0.07 | kPa | 100.24 | Calculated Property |
| Pvap | 1.92 | kPa | 120.34 | Calculated Property |
| Pvap | 18.27 | kPa | 140.43 | Calculated Property |
| Pvap | 92.53 | kPa | 160.53 | Calculated Property |
| Pvap | 314.43 | kPa | 180.62 | Calculated Property |
| Pvap | 817.30 | kPa | 200.72 | Calculated Property |
| Pvap | 1759.25 | kPa | 220.81 | Calculated Property |
| Pvap | 3299.43 | kPa | 240.91 | Calculated Property |
| Pvap | 5578.47 | kPa | 261.00 | Calculated Property |
| Pvap | [8.55e-04; 5429.09] | kPa | [80.15; 261.00] |
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 | 2.68924e+01 | |||
| Coefficient B | -2.06626e+03 | |||
| Coefficient C | -1.86514e+00 | |||
| Coefficient D | 3.69700e-08 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 80.15 | |||
| Temperature range, max. | 261.00 | |||
| Pvap | 8.55e-04 | kPa | 80.15 | Calculated Property |
| Pvap | 0.10 | kPa | 100.24 | Calculated Property |
| Pvap | 2.20 | kPa | 120.34 | Calculated Property |
| Pvap | 19.24 | kPa | 140.43 | Calculated Property |
| Pvap | 94.59 | kPa | 160.53 | Calculated Property |
| Pvap | 317.93 | kPa | 180.62 | Calculated Property |
| Pvap | 821.08 | kPa | 200.72 | Calculated Property |
| Pvap | 1754.25 | kPa | 220.81 | Calculated Property |
| Pvap | 3255.92 | kPa | 240.91 | Calculated Property |
| Pvap | 5429.09 | kPa | 261.00 | Calculated Property |
| Pvap | [0.12; 104.72] | kPa | [92.80; 162.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43598e+01 | |||
| Coefficient B | -1.64056e+03 | |||
| Coefficient C | 6.98200e+00 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 92.80 | |||
| Temperature range, max. | 162.00 | |||
| Pvap | 0.12 | kPa | 92.80 | Calculated Property |
| Pvap | 0.40 | kPa | 100.49 | Calculated Property |
| Pvap | 1.12 | kPa | 108.18 | Calculated Property |
| Pvap | 2.73 | kPa | 115.87 | Calculated Property |
| Pvap | 6.00 | kPa | 123.56 | Calculated Property |
| Pvap | 12.07 | kPa | 131.24 | Calculated Property |
| Pvap | 22.57 | kPa | 138.93 | Calculated Property |
| Pvap | 39.62 | kPa | 146.62 | Calculated Property |
| Pvap | 65.92 | kPa | 154.31 | Calculated Property |
| Pvap | 104.72 | kPa | 162.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1608.38; 556.91] | kg/m3 | [77.55; 261.00] |
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 | 1.26869e+02 | |||
| Coefficient B | 2.65440e-01 | |||
| Coefficient C | 2.61050e+02 | |||
| Coefficient D | 2.52390e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 77.55 | |||
| Temperature range, max. | 261.00 | |||
| ρl | 1608.38 | kg/m3 | 77.55 | Calculated Property |
| ρl | 1552.23 | kg/m3 | 97.93 | Calculated Property |
| ρl | 1492.82 | kg/m3 | 118.32 | Calculated Property |
| ρl | 1429.36 | kg/m3 | 138.70 | Calculated Property |
| ρl | 1360.68 | kg/m3 | 159.08 | Calculated Property |
| ρl | 1284.95 | kg/m3 | 179.47 | Calculated Property |
| ρl | 1199.02 | kg/m3 | 199.85 | Calculated Property |
| ρl | 1096.50 | kg/m3 | 220.23 | Calculated Property |
| ρl | 959.90 | kg/m3 | 240.62 | Calculated Property |
| ρl | 556.91 | kg/m3 | 261.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 2.67e-05] | N/m | [77.20; 261.00] |
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 | -8.38750e-03 | |||
| Coefficient B | 7.04170e+01 | |||
| Coefficient C | -4.45110e+00 | |||
| Coefficient D | 1.15550e-02 | |||
| Coefficient E | -5.30290e-05 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 77.20 | |||
| Temperature range, max. | 261.00 | |||
| γ | 0.04 | N/m | 77.20 | Calculated Property |
| γ | 0.04 | N/m | 97.62 | Calculated Property |
| γ | 0.03 | N/m | 118.04 | Calculated Property |
| γ | 0.03 | N/m | 138.47 | Calculated Property |
| γ | 0.02 | N/m | 158.89 | Calculated Property |
| γ | 0.02 | N/m | 179.31 | Calculated Property |
| γ | 0.01 | N/m | 199.73 | Calculated Property |
| γ | 0.01 | N/m | 220.16 | Calculated Property |
| γ | 0.00 | N/m | 240.58 | Calculated Property |
| γ | 2.67e-05 | N/m | 261.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.01; 0.07] | W/m×K | [161.85; 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 | 4.39070e-03 | |||
| Coefficient B | 4.78320e-01 | |||
| Coefficient C | 7.09480e+02 | |||
| Coefficient D | 2.33720e+02 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 161.85 | |||
| Temperature range, max. | 1000.00 | |||
| λ | 0.01 | W/m×K | 161.85 | Calculated Property |
| λ | 0.02 | W/m×K | 254.98 | Calculated Property |
| λ | 0.02 | W/m×K | 348.11 | Calculated Property |
| λ | 0.03 | W/m×K | 441.23 | Calculated Property |
| λ | 0.04 | W/m×K | 534.36 | Calculated Property |
| λ | 0.04 | W/m×K | 627.49 | Calculated Property |
| λ | 0.05 | W/m×K | 720.62 | Calculated Property |
| λ | 0.06 | W/m×K | 813.74 | Calculated Property |
| λ | 0.06 | W/m×K | 906.87 | Calculated Property |
| λ | 0.07 | W/m×K | 1000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.23; 0.23] | W/m×K | [77.35; 161.85] |
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 | 2.32550e-01 | |||
| Coefficient B | -6.78090e+02 | |||
| Coefficient C | -6.57050e+00 | |||
| Coefficient D | -7.49770e-02 | |||
| Coefficient E | 2.53910e-04 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 77.35 | |||
| Temperature range, max. | 161.85 | |||
| λ | 0.23 | W/m×K | 77.35 | Calculated Property |
| λ | 0.23 | W/m×K | 86.74 | Calculated Property |
| λ | 0.23 | W/m×K | 96.13 | Calculated Property |
| λ | 0.23 | W/m×K | 105.52 | Calculated Property |
| λ | 0.23 | W/m×K | 114.91 | Calculated Property |
| λ | 0.23 | W/m×K | 124.29 | Calculated Property |
| λ | 0.23 | W/m×K | 133.68 | Calculated Property |
| λ | 0.23 | W/m×K | 143.07 | Calculated Property |
| λ | 0.23 | W/m×K | 152.46 | Calculated Property |
| λ | 0.23 | W/m×K | 161.85 | Calculated Property |
Similar Compounds
Find more compounds similar to ozone.
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
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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