Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-3455.10; -3402.00] | kJ/mol |
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ΔcH°liquid | -3408.07 ± 0.85 | kJ/mol | NIST |
ΔcH°liquid | -3455.10 ± 1.30 | kJ/mol | NIST |
ΔcH°liquid | -3402.00 | kJ/mol | NIST |
ΔfH°gas | [-22.10; -14.50] | kJ/mol |
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ΔfH°gas | -14.50 ± 1.20 | kJ/mol | NIST |
ΔfH°gas | -22.10 | kJ/mol | NIST |
ΔfH°liquid | [-61.10; -33.90] | kJ/mol |
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ΔfH°liquid | -61.10 ± 1.10 | kJ/mol | NIST |
ΔfH°liquid | -33.90 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -33.90 ± 1.30 | kJ/mol | NIST |
ΔvapH° | [45.00; 46.50] | kJ/mol |
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ΔvapH° | 46.50 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 46.50 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 45.00 | kJ/mol | NIST |
IE | [8.77; 9.20] | eV |
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IE | 8.77 ± 0.02 | eV | NIST |
IE | 8.80 | eV | NIST |
IE | 9.20 | eV | NIST |
IE | 8.77 ± 0.02 | eV | NIST |
IE | 9.00 | eV | NIST |
log10WS | -5.95 | Crippen Calculated Property | |
logPoct/wat | 1.654 | Crippen Calculated Property | |
McVol | 92.980 | ml/mol | McGowan Calculated Property |
Pc | [4000.00; 4540.00] | kPa |
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Pc | 4000.00 | kPa | Critica... |
Pc | 4540.00 ± 300.00 | kPa | NIST |
ρc | 348.79 ± 20.25 | kg/m3 | NIST |
Inp | [142.80; 142.80] |
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|
Inp | 142.80 | NIST | |
Inp | 142.80 | NIST | |
Tboil | 452.91 | K | Joback Calculated Property |
Tc | 675.00 ± 3.00 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | 186.20 | J/mol×K | 298.15 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [322.74; 466.65] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.55620e+01 | |||
Coefficient B | -4.48522e+03 | |||
Coefficient C | -2.90940e+01 | |||
Temperature range, min. | 322.74 | |||
Temperature range, max. | 466.65 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 322.74 | Calculated Property |
Pvap | 2.93 | kPa | 338.73 | Calculated Property |
Pvap | 5.98 | kPa | 354.72 | Calculated Property |
Pvap | 11.39 | kPa | 370.71 | Calculated Property |
Pvap | 20.48 | kPa | 386.70 | Calculated Property |
Pvap | 35.04 | kPa | 402.69 | Calculated Property |
Pvap | 57.35 | kPa | 418.68 | Calculated Property |
Pvap | 90.30 | kPa | 434.67 | Calculated Property |
Pvap | 137.35 | kPa | 450.66 | Calculated Property |
Pvap | 202.63 | kPa | 466.65 | Calculated Property |
Pvap | [4.76e-03; 4090.52] | kPa | [243.15; 648.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.19158e+01 | |||
Coefficient B | -7.31927e+03 | |||
Coefficient C | -6.80993e+00 | |||
Coefficient D | 4.24507e-06 | |||
Temperature range, min. | 243.15 | |||
Temperature range, max. | 648.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 300 400 500 600 | ||||
Pvap | 4.76e-03 | kPa | 243.15 | Calculated Property |
Pvap | 0.18 | kPa | 288.13 | Calculated Property |
Pvap | 2.36 | kPa | 333.12 | Calculated Property |
Pvap | 15.59 | kPa | 378.10 | Calculated Property |
Pvap | 66.18 | kPa | 423.08 | Calculated Property |
Pvap | 207.89 | kPa | 468.07 | Calculated Property |
Pvap | 528.74 | kPa | 513.05 | Calculated Property |
Pvap | 1155.97 | kPa | 558.03 | Calculated Property |
Pvap | 2264.01 | kPa | 603.02 | Calculated Property |
Pvap | 4090.52 | kPa | 648.00 | Calculated Property |
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