Property | Value | Unit | Source |
---|---|---|---|
PAff | 823.70 | kJ/mol | NIST |
BasG | 797.40 | kJ/mol | NIST |
ΔcH°liquid | [-3908.00; -3780.00] | kJ/mol | |
ΔcH°liquid | -3816.60 ± 3.30 | kJ/mol | NIST |
ΔcH°liquid | -3817.50 ± 1.90 | kJ/mol | NIST |
ΔcH°liquid | Outlier -3908.00 ± 13.00 | kJ/mol | NIST |
ΔcH°liquid | -3789.40 ± 4.20 | kJ/mol | NIST |
ΔcH°liquid | -3780.80 ± 1.50 | kJ/mol | NIST |
ΔcH°liquid | -3780.00 ± 42.00 | kJ/mol | NIST |
ΔfH°gas | [-55.00; 73.00] | kJ/mol | |
ΔfH°gas | -17.20 ± 2.20 | kJ/mol | NIST |
ΔfH°gas | -45.30 ± 4.30 | kJ/mol | NIST |
ΔfH°gas | -18.10 ± 3.50 | kJ/mol | NIST |
ΔfH°gas | -17.70 ± 2.20 | kJ/mol | NIST |
ΔfH°gas | -53.90 ± 1.80 | kJ/mol | NIST |
ΔfH°gas | Outlier 73.00 ± 13.00 | kJ/mol | NIST |
ΔfH°gas | -55.00 ± 42.00 | kJ/mol | NIST |
ΔfH°liquid | [-87.00; 41.00] | kJ/mol | |
ΔfH°liquid | -49.20 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | -77.30 ± 4.20 | kJ/mol | NIST |
ΔfH°liquid | -50.10 ± 3.40 | kJ/mol | NIST |
ΔfH°liquid | -49.70 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | -85.90 ± 1.60 | kJ/mol | NIST |
ΔfH°liquid | Outlier 41.00 ± 13.00 | kJ/mol | NIST |
ΔfH°liquid | -87.00 ± 42.00 | kJ/mol | NIST |
ΔvapH° | [30.50; 33.10] | kJ/mol | |
ΔvapH° | 32.00 ± 0.80 | kJ/mol | NIST |
ΔvapH° | 31.10 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 32.80 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 30.50 | kJ/mol | NIST |
ΔvapH° | 33.10 | kJ/mol | NIST |
IE | [8.25; 9.75] | eV | |
IE | 8.89 ± 0.05 | eV | NIST |
IE | 8.93 ± 0.04 | eV | NIST |
IE | 8.90 ± 0.10 | eV | NIST |
IE | 8.76 ± 0.12 | eV | NIST |
IE | 8.76 ± 0.12 | eV | NIST |
IE | 8.76 ± 0.02 | eV | NIST |
IE | 8.25 ± 0.15 | eV | NIST |
IE | 9.70 | eV | NIST |
IE | 9.70 | eV | NIST |
IE | 9.75 | eV | NIST |
IE | 9.75 | eV | NIST |
Pc | 2981.30 ± 0.50 | kPa | NIST |
Inp | [602.00; 630.00] | ||
Inp | 604.50 | NIST | |
Inp | 603.30 | NIST | |
Inp | Outlier 630.00 | NIST | |
Inp | 604.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 602.00 | NIST | |
S°liquid | 310.80 | J/mol×K | NIST |
Tboil | 351.00 | K | NIST |
Tc | 521.81 ± 0.02 | K | NIST |
Tfus | 218.18 ± 0.05 | K | NIST |
Ttriple | 218.05 ± 0.02 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | 197.90 | J/mol×K | 298.15 | NIST |
ΔfusH | [9.23; 9.44] | kJ/mol | [218.05; 218.20] | |
ΔfusH | 9.23 | kJ/mol | 218.05 | NIST |
ΔfusH | 9.44 | kJ/mol | 218.18 | NIST |
ΔfusH | 9.23 | kJ/mol | 218.20 | NIST |
ΔvapH | [31.30; 33.40] | kJ/mol | [290.50; 353.00] | |
ΔvapH | 33.40 | kJ/mol | 290.50 | NIST |
ΔvapH | 31.60 | kJ/mol | 303.00 | NIST |
ΔvapH | 32.60 ± 0.20 | kJ/mol | 311.50 | NIST |
ΔvapH | 31.60 | kJ/mol | 331.50 | NIST |
ΔvapH | 31.30 | kJ/mol | 353.00 | NIST |
ΔfusS | [42.35; 43.26] | J/mol×K | [218.05; 218.18] | |
ΔfusS | 42.35 | J/mol×K | 218.05 | NIST |
ΔfusS | 43.26 | J/mol×K | 218.18 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [252.60; 375.66] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43838e+01 | |||
Coefficient B | -3.13250e+03 | |||
Coefficient C | -3.03770e+01 | |||
Temperature range, min. | 252.60 | |||
Temperature range, max. | 375.66 | |||
Pvap | 1.33 | kPa | 252.60 | Calculated Property |
Pvap | 3.02 | kPa | 266.27 | Calculated Property |
Pvap | 6.25 | kPa | 279.95 | Calculated Property |
Pvap | 11.99 | kPa | 293.62 | Calculated Property |
Pvap | 21.58 | kPa | 307.29 | Calculated Property |
Pvap | 36.74 | kPa | 320.97 | Calculated Property |
Pvap | 59.65 | kPa | 334.64 | Calculated Property |
Pvap | 92.87 | kPa | 348.31 | Calculated Property |
Pvap | 139.41 | kPa | 361.99 | Calculated Property |
Pvap | 202.66 | kPa | 375.66 | Calculated Property |
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