Property | Value | Unit | Source |
---|---|---|---|
ω | -0.0080 | KDB | |
IE | [10.75; 10.75] | eV | |
IE | 10.75 | eV | NIST |
IE | 10.75 | eV | NIST |
Pc | 6280.00 | kPa | KDB |
Tboil | 211.40 | K | KDB |
Tc | 377.00 | K | KDB |
Tfus | 202.00 | K | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ρl | 4400.00 | kg/m3 | 211.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.00e-03; 6279.41] | kPa | [110.15; 377.00] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.31363e+01 | |||
Coefficient B | -1.50053e+03 | |||
Coefficient C | -3.52900e+01 | |||
Temperature range, min. | 110.15 | |||
Temperature range, max. | 377.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 6000 200 300 | ||||
Pvap | 1.00e-03 | kPa | 110.15 | Calculated Property |
Pvap | 0.29 | kPa | 139.80 | Calculated Property |
Pvap | 7.04 | kPa | 169.45 | Calculated Property |
Pvap | 53.31 | kPa | 199.10 | Calculated Property |
Pvap | 217.02 | kPa | 228.75 | Calculated Property |
Pvap | 608.35 | kPa | 258.40 | Calculated Property |
Pvap | 1339.01 | kPa | 288.05 | Calculated Property |
Pvap | 2497.30 | kPa | 317.70 | Calculated Property |
Pvap | 4137.31 | kPa | 347.35 | Calculated Property |
Pvap | 6279.41 | kPa | 377.00 | Calculated Property |
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