- InChI
- InChI=1S/CCl2O/c2-1(3)4
- InChI Key
- YGYAWVDWMABLBF-UHFFFAOYSA-N
- Formula
- CCl2O
- SMILES
- O=C(Cl)Cl
- Molecular Weight1
- 98.92
- CAS
- 75-44-5
- Other Names
-
- CG
- COCl2
- Carbon dichloride oxide
- Carbon oxychloride
- Carbone (oxychlorure de)
- Carbonic chloride
- Carbonic dichloride
- Carbonio (ossicloruro di)
- Carbonyl chloride
- Carbonyl dichloride
- Carbonylchlorid
- Chloroformyl chloride
- Dichloroformaldehyde
- Fosgeen
- Fosgen
- Fosgene
- Koolstofoxychloride
- NCI-C60219
- Phosgen
- Rcra waste number P095
- UN 1076
- ω : Acentric Factor.
- ΔcH°gas : Standard gas enthalpy of combustion (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).
- 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 standard conditions (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).
- ρg : Gas Density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- 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.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.2013; 0.2050] |
|
|
| ω | 0.2013 | ChemSep v8.3 pure component data | |
| ω | 0.2050 | KDB | |
| ΔcH°gas | -108.60 ± 0.42 | kJ/mol | NIST |
| μ | [1.10; 1.17] | debye |
|
| μ | 1.17 | debye | ChemSep v8.3 pure component data |
| μ | 1.10 | debye | KDB |
| ΔfG° | [-206.90; -204.79] | kJ/mol |
|
| ΔfG° | -204.79 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfG° | -206.90 | kJ/mol | KDB |
| ΔfH°gas | [-221.10; -209.50] | kJ/mol |
|
| ΔfH°gas | -218.90 | kJ/mol | ChemSep v8.3 pure component data |
| ΔfH°gas | -221.10 | kJ/mol | KDB |
| ΔfH°gas | -220.10 ± 0.96 | kJ/mol | NIST |
| ΔfH°gas | -219.10 ± 0.59 | kJ/mol | NIST |
| ΔfH°gas | -209.50 ± 1.20 | kJ/mol | NIST |
| ΔfusH° | 8.34 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 22.08 | kJ/mol | Relay (1.0) Calculated Property |
| IE | [11.20; 11.84] | eV |
|
| IE | 11.20 | eV | NIST |
| IE | 11.55 ± 0.02 | eV | NIST |
| IE | 11.70 | eV | NIST |
| IE | 11.84 | eV | NIST |
| logPoct/wat | 1.584 | Crippen Calculated Property | |
| McVol | 51.000 | ml/mol | McGowan Calculated Property |
| Pc | [5670.00; 5674.20] | kPa |
|
| Pc | 5674.20 | kPa | ChemSep v8.3 pure component data |
| Pc | 5670.00 | kPa | Air Liquide Gas Encyclopedia |
| Pc | 5674.00 | kPa | KDB |
| Ptriple | 9.21e-04 | kPa | ChemSep v8.3 pure component data |
| Inp | [416.00; 425.00] |
|
|
| Inp | 416.00 | NIST | |
| Inp | 425.00 | NIST | |
| Inp | 425.00 | NIST | |
| S°liquid | [192.80; 198.11] | J/mol×K |
|
| S°liquid | 192.80 | J/mol×K | NIST |
| S°liquid | 198.11 | J/mol×K | NIST |
| Tboil | [280.70; 280.71] | K |
|
| Tboil | 280.71 | K | ChemSep v8.3 pure component data |
| Tboil | 280.70 | K | Air Liquide Gas Encyclopedia |
| Tboil | 280.71 | K | KDB |
| Tc | [455.00; 455.15] | K |
|
| Tc | 455.00 | K | ChemSep v8.3 pure component data |
| Tc | 455.15 | K | Air Liquide Gas Encyclopedia |
| Tc | 455.15 | K | KDB |
| Tfus | [145.00; 145.37] | K |
|
| Tfus | 145.37 | K | ChemSep v8.3 pure component data |
| Tfus | 145.15 | K | Air Liquide Gas Encyclopedia |
| Tfus | 145.00 | K | KDB |
| Ttriple | [139.19; 145.37] | K |
|
| Ttriple | 145.37 | K | ChemSep v8.3 pure component data |
| Ttriple | 139.19 ± 0.20 | K | NIST |
| Ttriple | 145.37 ± 0.02 | K | NIST |
| Ttriple | 142.09 ± 0.05 | K | NIST |
| Ttriple | 145.37 ± 0.02 | K | NIST |
| Ttriple | 145.37 ± 0.02 | K | NIST |
| UQi | 2.08 | ChemSep v8.3 pure component data | |
| URi | 2.30 | ChemSep v8.3 pure component data | |
| Vc | [0.190; 0.190] | m3/kmol |
|
| Vc | 0.190 | m3/kmol | ChemSep v8.3 pure component data |
| Vc | 0.190 | m3/kmol | KDB |
| Zc | [0.2850000; 0.2850230] |
|
|
| Zc | 0.2850000 | ChemSep v8.3 pure component data | |
| Zc | 0.2850230 | KDB |
Cheméo can also estimate Log10 of Water solubility in mol/l for this compound, but it falls outside the models' validated range, so it is not shown here. Open the prediction tool to compute it on demand.
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [100.79; 102.59] | J/mol×K | [160.55; 280.00] |
|
| Cp,liquid | 102.59 | J/mol×K | 160.55 | NIST |
| Cp,liquid | 100.79 | J/mol×K | 280.00 | NIST |
| ΔfusH | [5.73; 5.74] | kJ/mol | [145.30; 145.37] |
|
| ΔfusH | 5.73 | kJ/mol | 145.30 | NIST |
| ΔfusH | 5.73 | kJ/mol | 145.30 | NIST |
| ΔfusH | 5.74 | kJ/mol | 145.37 | NIST |
| ΔfusH | 5.74 | kJ/mol | 145.37 | NIST |
| ΔvapH | [24.40; 27.00] | kJ/mol | [226.50; 430.50] |
|
| ΔvapH | 25.80 | kJ/mol | 226.50 | NIST |
| ΔvapH | 27.00 | kJ/mol | 231.50 | NIST |
| ΔvapH | 27.00 | kJ/mol | 231.50 | NIST |
| ΔvapH | 25.70 | kJ/mol | 260.50 | NIST |
| ΔvapH | 24.40 | kJ/mol | 280.70 | Air Liquide Gas Encyclopedia |
| ΔvapH | 24.40 | kJ/mol | 280.71 | NIST |
| ΔvapH | 24.40 | kJ/mol | 280.71 | NIST |
| ΔvapH | 24.50 | kJ/mol | 310.50 | NIST |
| ΔvapH | 24.50 | kJ/mol | 374.00 | NIST |
| ΔvapH | 24.40 | kJ/mol | 430.50 | NIST |
| ρg | 4.35 | kg/m3 | 280.70 | Air Liquide Gas Encyclopedia |
| ρl | [1381.00; 1403.00] | kg/m3 | [280.70; 293.00] |
|
| ρl | 1403.00 | kg/m3 | 280.70 | Air Liquide Gas Encyclopedia |
| ρl | 1381.00 | kg/m3 | 293.00 | KDB |
| ΔfusS | [39.46; 39.46] | J/mol×K | [145.37; 145.37] |
|
| ΔfusS | 39.46 | J/mol×K | 145.37 | NIST |
| ΔfusS | 39.46 | J/mol×K | 145.37 | NIST |
| ΔvapS | [86.93; 86.93] | J/mol×K | [280.71; 280.71] |
|
| ΔvapS | 86.93 | J/mol×K | 280.71 | NIST |
| ΔvapS | 86.93 | J/mol×K | 280.71 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [36.47; 80.27] | J/mol×K | [100.00; 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 | 3.25060e+01 | |||
| Coefficient B | -2.82160e+02 | |||
| Coefficient C | 4.21624e+00 | |||
| Coefficient D | -1.76360e-04 | |||
| Coefficient E | 4.56510e-08 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 100.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 36.47 | J/mol×K | 100.00 | Calculated Property |
| Cp,gas | 54.05 | J/mol×K | 255.56 | Calculated Property |
| Cp,gas | 64.49 | J/mol×K | 411.11 | Calculated Property |
| Cp,gas | 70.33 | J/mol×K | 566.67 | Calculated Property |
| Cp,gas | 73.85 | J/mol×K | 722.22 | Calculated Property |
| Cp,gas | 76.11 | J/mol×K | 877.78 | Calculated Property |
| Cp,gas | 77.64 | J/mol×K | 1033.33 | Calculated Property |
| Cp,gas | 78.74 | J/mol×K | 1188.89 | Calculated Property |
| Cp,gas | 79.58 | J/mol×K | 1344.44 | Calculated Property |
| Cp,gas | 80.27 | J/mol×K | 1500.00 | Calculated Property |
| Cp,gas | [57.68; 71.05] | J/mol×K | [298.00; 600.00] |
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 | 3.66480e+01 | |||
| Coefficient B | 1.15127e+02 | |||
| Coefficient C | -1.28621e+02 | |||
| Coefficient D | 5.76869e+01 | |||
| Coefficient E | -2.99915e-01 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-236.1052, G=297.3410, H=-220.0784; Data last reviewed in June, 1961 | |||
| Temperature range, min. | 298.00 | |||
| Temperature range, max. | 600.00 | |||
| Cp,gas | 57.68 | J/mol×K | 298.00 | Calculated Property |
| Cp,gas | 60.05 | J/mol×K | 331.56 | Calculated Property |
| Cp,gas | 62.09 | J/mol×K | 365.11 | Calculated Property |
| Cp,gas | 63.87 | J/mol×K | 398.67 | Calculated Property |
| Cp,gas | 65.43 | J/mol×K | 432.22 | Calculated Property |
| Cp,gas | 66.81 | J/mol×K | 465.78 | Calculated Property |
| Cp,gas | 68.04 | J/mol×K | 499.33 | Calculated Property |
| Cp,gas | 69.15 | J/mol×K | 532.89 | Calculated Property |
| Cp,gas | 70.14 | J/mol×K | 566.44 | Calculated Property |
| Cp,gas | 71.05 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | [70.77; 83.06] | J/mol×K | [600.00; 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 | 7.81977e+01 | |||
| Coefficient B | 3.28691e+00 | |||
| Coefficient C | -7.57840e-01 | |||
| Coefficient D | 5.79320e-02 | |||
| Coefficient E | -3.29201e+00 | |||
| Reference | Chase, 1998 | |||
| Comment | F=-253.2500, G=362.6110, H=-220.0784; Data last reviewed in June, 1961 | |||
| Temperature range, min. | 600.00 | |||
| Temperature range, max. | 6000.00 | |||
| Cp,gas | 70.77 | J/mol×K | 600.00 | Calculated Property |
| Cp,gas | 78.86 | J/mol×K | 1200.00 | Calculated Property |
| Cp,gas | 80.98 | J/mol×K | 1800.00 | Calculated Property |
| Cp,gas | 81.95 | J/mol×K | 2400.00 | Calculated Property |
| Cp,gas | 82.44 | J/mol×K | 3000.00 | Calculated Property |
| Cp,gas | 82.66 | J/mol×K | 3600.00 | Calculated Property |
| Cp,gas | 82.74 | J/mol×K | 4200.00 | Calculated Property |
| Cp,gas | 82.78 | J/mol×K | 4800.00 | Calculated Property |
| Cp,gas | 82.86 | J/mol×K | 5400.00 | Calculated Property |
| Cp,gas | 83.06 | J/mol×K | 6000.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [101.24; 101.24] | J/mol×K | [139.95; 280.00] |
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 | 1.01240e+02 | |||
| Coefficient B | -2.02030e+05 | |||
| Coefficient C | 1.89402e+02 | |||
| Coefficient D | 2.17040e+00 | |||
| Coefficient E | -1.55120e-03 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 139.95 | |||
| Temperature range, max. | 280.00 | |||
| Cp,liquid | 101.24 | J/mol×K | 139.95 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 155.51 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 171.07 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 186.63 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 202.19 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 217.76 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 233.32 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 248.88 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 264.44 | Calculated Property |
| Cp,liquid | 101.24 | J/mol×K | 280.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0009137; 0.0005489] | Pa×s | [224.53; 280.71] |
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 | -7.89510e+02 | |||
| Coefficient B | 2.24740e+04 | |||
| Coefficient C | 1.29100e+02 | |||
| Coefficient D | -3.27890e-04 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 224.53 | |||
| Temperature range, max. | 280.71 | |||
| η | 0.0009137 | Pa×s | 224.53 | Calculated Property |
| η | 0.0008274 | Pa×s | 230.77 | Calculated Property |
| η | 0.0007664 | Pa×s | 237.01 | Calculated Property |
| η | 0.0007217 | Pa×s | 243.26 | Calculated Property |
| η | 0.0006872 | Pa×s | 249.50 | Calculated Property |
| η | 0.0006586 | Pa×s | 255.74 | Calculated Property |
| η | 0.0006326 | Pa×s | 261.98 | Calculated Property |
| η | 0.0006068 | Pa×s | 268.23 | Calculated Property |
| η | 0.0005793 | Pa×s | 274.47 | Calculated Property |
| η | 0.0005489 | Pa×s | 280.71 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [31.79; 10.07] | kJ/mol | [145.37; 438.70] |
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 | 4.36725e+01 | |||
| Coefficient B | 1.08182e+00 | |||
| Coefficient C | -7.73774e-01 | |||
| Coefficient D | -1.93700e-01 | |||
| Coefficient E | 3.17951e-01 | |||
| Critical temperature, Tc (K) | 4.55000e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 438.70 | |||
| ΔvapH | 31.79 | kJ/mol | 145.37 | Calculated Property |
| ΔvapH | 29.83 | kJ/mol | 177.96 | Calculated Property |
| ΔvapH | 28.03 | kJ/mol | 210.55 | Calculated Property |
| ΔvapH | 26.34 | kJ/mol | 243.15 | Calculated Property |
| ΔvapH | 24.68 | kJ/mol | 275.74 | Calculated Property |
| ΔvapH | 22.97 | kJ/mol | 308.33 | Calculated Property |
| ΔvapH | 21.06 | kJ/mol | 340.92 | Calculated Property |
| ΔvapH | 18.74 | kJ/mol | 373.52 | Calculated Property |
| ΔvapH | 15.55 | kJ/mol | 406.11 | Calculated Property |
| ΔvapH | 10.07 | kJ/mol | 438.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [9.20e-04; 5712.92] | kPa | [145.37; 455.00] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44269e+01 | |||
| Coefficient B | -2.44909e+03 | |||
| Coefficient C | -3.10200e+01 | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 455.00 | |||
| Pvap | 9.20e-04 | kPa | 145.37 | Calculated Property |
| Pvap | 0.13 | kPa | 179.77 | Calculated Property |
| Pvap | 2.87 | kPa | 214.18 | Calculated Property |
| Pvap | 23.80 | kPa | 248.58 | Calculated Property |
| Pvap | 110.71 | kPa | 282.98 | Calculated Property |
| Pvap | 355.89 | kPa | 317.39 | Calculated Property |
| Pvap | 890.58 | kPa | 351.79 | Calculated Property |
| Pvap | 1865.78 | kPa | 386.19 | Calculated Property |
| Pvap | 3430.19 | kPa | 420.60 | Calculated Property |
| Pvap | 5712.92 | kPa | 455.00 | Calculated Property |
| Pvap | [9.80e-04; 5771.59] | kPa | [145.37; 455.15] |
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 | 7.41279e+01 | |||
| Coefficient B | -5.11211e+03 | |||
| Coefficient C | -9.26705e+00 | |||
| Coefficient D | 1.19936e-05 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 455.15 | |||
| Pvap | 9.80e-04 | kPa | 145.37 | Calculated Property |
| Pvap | 0.13 | kPa | 179.79 | Calculated Property |
| Pvap | 2.94 | kPa | 214.21 | Calculated Property |
| Pvap | 24.33 | kPa | 248.63 | Calculated Property |
| Pvap | 111.03 | kPa | 283.05 | Calculated Property |
| Pvap | 348.05 | kPa | 317.47 | Calculated Property |
| Pvap | 853.92 | kPa | 351.89 | Calculated Property |
| Pvap | 1779.63 | kPa | 386.31 | Calculated Property |
| Pvap | 3324.18 | kPa | 420.73 | Calculated Property |
| Pvap | 5771.59 | kPa | 455.15 | Calculated Property |
| Pvap | [3.27; 102.46] | kPa | [215.53; 281.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39330e+01 | |||
| Coefficient B | -2.25409e+03 | |||
| Coefficient C | -3.87170e+01 | |||
| Reference | Giauque and Jones, 1948 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 215.53 | |||
| Temperature range, max. | 281.00 | |||
| Pvap | 3.27 | kPa | 215.53 | Calculated Property |
| Pvap | 5.41 | kPa | 222.80 | Calculated Property |
| Pvap | 8.62 | kPa | 230.08 | Calculated Property |
| Pvap | 13.27 | kPa | 237.35 | Calculated Property |
| Pvap | 19.81 | kPa | 244.63 | Calculated Property |
| Pvap | 28.78 | kPa | 251.90 | Calculated Property |
| Pvap | 40.79 | kPa | 259.18 | Calculated Property |
| Pvap | 56.55 | kPa | 266.45 | Calculated Property |
| Pvap | 76.82 | kPa | 273.73 | Calculated Property |
| Pvap | 102.46 | kPa | 281.00 | Calculated Property |
| Pvap | [0.13; 101.12] | kPa | [180.30; 281.40] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.36978e+01 | |||
| Coefficient B | -2.17671e+03 | |||
| Coefficient C | -4.17150e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 180.30 | |||
| Temperature range, max. | 281.40 | |||
| Pvap | 0.13 | kPa | 180.30 | Calculated Property |
| Pvap | 0.44 | kPa | 191.53 | Calculated Property |
| Pvap | 1.20 | kPa | 202.77 | Calculated Property |
| Pvap | 2.90 | kPa | 214.00 | Calculated Property |
| Pvap | 6.28 | kPa | 225.23 | Calculated Property |
| Pvap | 12.44 | kPa | 236.47 | Calculated Property |
| Pvap | 22.89 | kPa | 247.70 | Calculated Property |
| Pvap | 39.53 | kPa | 258.93 | Calculated Property |
| Pvap | 64.70 | kPa | 270.17 | Calculated Property |
| Pvap | 101.12 | kPa | 281.40 | Calculated Property |
| Pvap | [101.52; 5006.08] | kPa | [281.40; 447.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.44396e+01 | |||
| Coefficient B | -2.47001e+03 | |||
| Coefficient C | -2.98550e+01 | |||
| Reference | Stull, 1947 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 281.40 | |||
| Temperature range, max. | 447.00 | |||
| Pvap | 101.52 | kPa | 281.40 | Calculated Property |
| Pvap | 198.26 | kPa | 299.80 | Calculated Property |
| Pvap | 355.48 | kPa | 318.20 | Calculated Property |
| Pvap | 594.26 | kPa | 336.60 | Calculated Property |
| Pvap | 937.29 | kPa | 355.00 | Calculated Property |
| Pvap | 1407.92 | kPa | 373.40 | Calculated Property |
| Pvap | 2029.14 | kPa | 391.80 | Calculated Property |
| Pvap | 2822.86 | kPa | 410.20 | Calculated Property |
| Pvap | 3809.21 | kPa | 428.60 | Calculated Property |
| Pvap | 5006.08 | kPa | 447.00 | Calculated Property |
| Pvap | [3.27; 102.46] | kPa | [215.53; 281.00] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.39330e+01 | |||
| Coefficient B | -2.25409e+03 | |||
| Coefficient C | -3.87170e+01 | |||
| Reference | Giauque and Jones, 1948, 2 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 215.53 | |||
| Temperature range, max. | 281.00 | |||
| Pvap | 3.27 | kPa | 215.53 | Calculated Property |
| Pvap | 5.41 | kPa | 222.80 | Calculated Property |
| Pvap | 8.62 | kPa | 230.08 | Calculated Property |
| Pvap | 13.27 | kPa | 237.35 | Calculated Property |
| Pvap | 19.81 | kPa | 244.63 | Calculated Property |
| Pvap | 28.78 | kPa | 251.90 | Calculated Property |
| Pvap | 40.79 | kPa | 259.18 | Calculated Property |
| Pvap | 56.55 | kPa | 266.45 | Calculated Property |
| Pvap | 76.82 | kPa | 273.73 | Calculated Property |
| Pvap | 102.46 | kPa | 281.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1663.64; 871.02] | kg/m3 | [145.37; 438.70] |
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 | 1.45318e+02 | |||
| Coefficient B | 2.76800e-01 | |||
| Coefficient C | 4.55000e+02 | |||
| Coefficient D | 2.79650e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 438.70 | |||
| ρl | 1663.64 | kg/m3 | 145.37 | Calculated Property |
| ρl | 1605.90 | kg/m3 | 177.96 | Calculated Property |
| ρl | 1545.31 | kg/m3 | 210.55 | Calculated Property |
| ρl | 1481.24 | kg/m3 | 243.15 | Calculated Property |
| ρl | 1412.75 | kg/m3 | 275.74 | Calculated Property |
| ρl | 1338.45 | kg/m3 | 308.33 | Calculated Property |
| ρl | 1256.09 | kg/m3 | 340.92 | Calculated Property |
| ρl | 1161.44 | kg/m3 | 373.52 | Calculated Property |
| ρl | 1044.95 | kg/m3 | 406.11 | Calculated Property |
| ρl | 871.02 | kg/m3 | 438.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [145.37; 438.70] |
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 | -1.61390e-02 | |||
| Coefficient B | 2.85610e+01 | |||
| Coefficient C | -2.97890e+00 | |||
| Coefficient D | 5.85570e-04 | |||
| Coefficient E | -7.21420e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 438.70 | |||
| γ | 0.04 | N/m | 145.37 | Calculated Property |
| γ | 0.04 | N/m | 177.96 | Calculated Property |
| γ | 0.03 | N/m | 210.55 | Calculated Property |
| γ | 0.03 | N/m | 243.15 | Calculated Property |
| γ | 0.02 | N/m | 275.74 | Calculated Property |
| γ | 0.02 | N/m | 308.33 | Calculated Property |
| γ | 0.01 | N/m | 340.92 | Calculated Property |
| γ | 0.01 | N/m | 373.52 | Calculated Property |
| γ | 0.00 | N/m | 406.11 | Calculated Property |
| γ | 0.00 | N/m | 438.70 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.00; 0.04] | W/m×K | [145.37; 800.00] |
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 | 2.43680e-05 | |||
| Coefficient B | 1.14230e+00 | |||
| Coefficient C | 2.46560e+02 | |||
| Coefficient D | 4.29650e+03 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 800.00 | |||
| λ | 0.00 | W/m×K | 145.37 | Calculated Property |
| λ | 0.01 | W/m×K | 218.11 | Calculated Property |
| λ | 0.01 | W/m×K | 290.84 | Calculated Property |
| λ | 0.01 | W/m×K | 363.58 | Calculated Property |
| λ | 0.02 | W/m×K | 436.32 | Calculated Property |
| λ | 0.02 | W/m×K | 509.05 | Calculated Property |
| λ | 0.02 | W/m×K | 581.79 | Calculated Property |
| λ | 0.03 | W/m×K | 654.53 | Calculated Property |
| λ | 0.03 | W/m×K | 727.26 | Calculated Property |
| λ | 0.04 | W/m×K | 800.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.17; 0.13] | W/m×K | [145.37; 312.11] |
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 | 2.50610e-03 | |||
| Coefficient B | 3.56740e+00 | |||
| Coefficient C | -1.65920e+00 | |||
| Coefficient D | -7.95200e-04 | |||
| Coefficient E | -1.80880e-06 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 145.37 | |||
| Temperature range, max. | 312.11 | |||
| λ | 0.17 | W/m×K | 145.37 | Calculated Property |
| λ | 0.17 | W/m×K | 163.90 | Calculated Property |
| λ | 0.16 | W/m×K | 182.42 | Calculated Property |
| λ | 0.16 | W/m×K | 200.95 | Calculated Property |
| λ | 0.15 | W/m×K | 219.48 | Calculated Property |
| λ | 0.15 | W/m×K | 238.00 | Calculated Property |
| λ | 0.14 | W/m×K | 256.53 | Calculated Property |
| λ | 0.14 | W/m×K | 275.06 | Calculated Property |
| λ | 0.13 | W/m×K | 293.58 | Calculated Property |
| λ | 0.13 | W/m×K | 312.11 | Calculated Property |
Similar Compounds
Find more compounds similar to Phosgene.
Sources
- Air Liquide Gas Encyclopedia
- Cheméo Relay (1.0)
- 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
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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