Property | Value | Unit | Source |
---|---|---|---|
PAff | 833.00 | kJ/mol | NIST |
BasG | 798.50 | kJ/mol | NIST |
ΔcH°liquid | -1614.60 ± 6.30 | kJ/mol | NIST |
ΔfH°gas | -723.90 ± 6.70 | kJ/mol | NIST |
ΔfH°liquid | -764.10 ± 6.70 | kJ/mol | NIST |
ΔvapH° | [38.10; 40.20] | kJ/mol | |
ΔvapH° | 40.20 ± 0.80 | kJ/mol | NIST |
ΔvapH° | 38.10 ± 0.40 | kJ/mol | NIST |
IE | [7.90; 8.60] | eV | |
IE | 7.90 ± 0.03 | eV | NIST |
IE | 8.40 ± 0.20 | eV | NIST |
IE | 7.98 ± 0.01 | eV | NIST |
IE | 8.00 ± 0.08 | eV | NIST |
IE | 7.96 ± 0.02 | eV | NIST |
IE | 7.95 ± 0.03 | eV | NIST |
IE | 8.60 | eV | NIST |
IE | 8.60 | eV | NIST |
IE | 8.60 | eV | NIST |
Tboil | 376.00 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔvapH | [37.60; 40.10] | kJ/mol | [279.00; 322.00] | |
ΔvapH | 40.10 ± 0.50 | kJ/mol | 279.00 | NIST |
ΔvapH | 39.00 | kJ/mol | 309.50 | NIST |
ΔvapH | 37.60 | kJ/mol | 322.00 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.68] | kPa | [278.04; 397.85] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.84775e+01 | |||
Coefficient B | -5.71116e+03 | |||
Coefficient C | 3.59370e+01 | |||
Temperature range, min. | 278.04 | |||
Temperature range, max. | 397.85 | |||
Pvap | 1.33 | kPa | 278.04 | Calculated Property |
Pvap | 2.79 | kPa | 291.35 | Calculated Property |
Pvap | 5.53 | kPa | 304.66 | Calculated Property |
Pvap | 10.38 | kPa | 317.98 | Calculated Property |
Pvap | 18.64 | kPa | 331.29 | Calculated Property |
Pvap | 32.12 | kPa | 344.60 | Calculated Property |
Pvap | 53.34 | kPa | 357.91 | Calculated Property |
Pvap | 85.69 | kPa | 371.23 | Calculated Property |
Pvap | 133.60 | kPa | 384.54 | Calculated Property |
Pvap | 202.68 | kPa | 397.85 | Calculated Property |
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