Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -5314.60 ± 2.00 | kJ/mol | NIST |
ΔfH°gas | 161.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | 93.30 | kJ/mol | NIST |
ΔvapH° | [67.70; 67.70] | kJ/mol | |
ΔvapH° | 67.70 ± 1.80 | kJ/mol | NIST |
ΔvapH° | 67.70 | kJ/mol | NIST |
ΔvapH° | 67.70 ± 1.80 | kJ/mol | NIST |
log10WS | -3.52 | Crippen Calculated Property | |
logPoct/wat | 2.543 | Crippen Calculated Property | |
McVol | 118.520 | ml/mol | McGowan Calculated Property |
Inp | [229.82; 1358.00] | ||
Inp | 1343.00 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 1343.00 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 1335.00 | NIST | |
Inp | 1321.20 | NIST | |
Inp | 1318.00 | NIST | |
Inp | 1358.00 | NIST | |
Inp | 230.75 | NIST | |
Inp | 229.82 | NIST | |
Inp | 230.75 | NIST | |
Inp | 1321.20 | NIST | |
Inp | 1343.00 | NIST | |
I | [1995.00; 2062.00] | ||
I | 1995.00 | NIST | |
I | 2020.00 | NIST | |
I | 1995.00 | NIST | |
I | 2020.00 | NIST | |
I | 1995.00 | NIST | |
I | 2020.00 | NIST | |
I | 2016.00 | NIST | |
I | Outlier 2062.00 | NIST | |
Tboil | [525.65; 538.20] | K | |
Tboil | 531.80 | K | NIST |
Tboil | 538.20 ± 0.20 | K | NIST |
Tboil | 530.15 ± 0.70 | K | NIST |
Tboil | 538.18 ± 0.05 | K | NIST |
Tboil | 527.00 ± 2.00 | K | NIST |
Tboil | 532.40 ± 0.30 | K | NIST |
Tboil | 532.15 ± 1.00 | K | NIST |
Tboil | 525.65 ± 3.00 | K | NIST |
Tfus | [247.15; 305.60] | K | |
Tfus | 247.15 ± 0.30 | K | NIST |
Tfus | 305.60 ± 0.20 | K | NIST |
Tfus | 305.60 ± 0.40 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔvapH | 56.10 | kJ/mol | 496.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [397.09; 565.46] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.44514e+01 | |||
Coefficient B | -4.33852e+03 | |||
Coefficient C | -9.07810e+01 | |||
Temperature range, min. | 397.09 | |||
Temperature range, max. | 565.46 | |||
Pvap | 1.33 | kPa | 397.09 | Calculated Property |
Pvap | 3.01 | kPa | 415.80 | Calculated Property |
Pvap | 6.23 | kPa | 434.51 | Calculated Property |
Pvap | 11.95 | kPa | 453.21 | Calculated Property |
Pvap | 21.51 | kPa | 471.92 | Calculated Property |
Pvap | 36.63 | kPa | 490.63 | Calculated Property |
Pvap | 59.50 | kPa | 509.34 | Calculated Property |
Pvap | 92.70 | kPa | 528.04 | Calculated Property |
Pvap | 139.28 | kPa | 546.75 | Calculated Property |
Pvap | 202.65 | kPa | 565.46 | Calculated Property |
Pvap | [12.53; 103.39] | kPa | [459.15; 539.15] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.36389e+02 | |||
Coefficient B | -1.34466e+04 | |||
Coefficient C | -1.72949e+01 | |||
Coefficient D | 6.79359e-06 | |||
Temperature range, min. | 459.15 | |||
Temperature range, max. | 539.15 | |||
Pvap | 12.53 | kPa | 459.15 | Calculated Property |
Pvap | 16.59 | kPa | 468.04 | Calculated Property |
Pvap | 21.67 | kPa | 476.93 | Calculated Property |
Pvap | 27.96 | kPa | 485.82 | Calculated Property |
Pvap | 35.65 | kPa | 494.71 | Calculated Property |
Pvap | 44.96 | kPa | 503.59 | Calculated Property |
Pvap | 56.12 | kPa | 512.48 | Calculated Property |
Pvap | 69.40 | kPa | 521.37 | Calculated Property |
Pvap | 85.06 | kPa | 530.26 | Calculated Property |
Pvap | 103.39 | kPa | 539.15 | Calculated Property |
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