Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4060 | KDB | |
ΔcH°liquid | -5314.30 ± 2.10 | kJ/mol | NIST |
ΔfH°gas | 159.10 ± 3.10 | kJ/mol | NIST |
ΔfH°liquid | 93.00 ± 2.50 | kJ/mol | NIST |
ΔfusH° | 12.52 | kJ/mol | The the... |
ΔvapH° | [62.60; 66.10] | kJ/mol | |
ΔvapH° | 62.60 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 66.10 ± 1.90 | kJ/mol | NIST |
ΔvapH° | 66.10 | kJ/mol | NIST |
ΔvapH° | 66.10 ± 1.90 | kJ/mol | NIST |
log10WS | -3.52 | Crippen Calculated Property | |
logPoct/wat | 2.543 | Crippen Calculated Property | |
McVol | 118.520 | ml/mol | McGowan Calculated Property |
Pc | 4900.00 | kPa | KDB |
Inp | [223.47; 1313.00] | ||
Inp | 1294.00 | NIST | |
Inp | 1308.00 | NIST | |
Inp | 1294.00 | NIST | |
Inp | 1308.00 | NIST | |
Inp | 1293.00 | NIST | |
Inp | 1277.50 | NIST | |
Inp | 1312.00 | NIST | |
Inp | 1287.20 | NIST | |
Inp | 1287.20 | NIST | |
Inp | 1311.00 | NIST | |
Inp | 1313.00 | NIST | |
Inp | 223.47 | NIST | |
Inp | 223.94 | NIST | |
Inp | 224.13 | NIST | |
Inp | 223.47 | NIST | |
I | [1924.00; 1971.00] | ||
I | 1924.00 | NIST | |
I | 1946.00 | NIST | |
I | 1924.00 | NIST | |
I | 1946.00 | NIST | |
I | 1924.00 | NIST | |
I | 1946.00 | NIST | |
I | 1940.00 | NIST | |
I | 1969.00 | NIST | |
I | 1971.00 | NIST | |
I | 1970.00 | NIST | |
Tboil | [518.95; 521.20] | K | |
Tboil | 520.90 | K | KDB |
Tboil | 521.20 | K | NIST |
Tboil | 520.90 ± 0.17 | K | NIST |
Tboil | 521.15 ± 0.70 | K | NIST |
Tboil | 520.90 ± 0.07 | K | NIST |
Tboil | 519.80 ± 0.30 | K | NIST |
Tboil | 520.00 ± 10.00 | K | NIST |
Tboil | 519.00 ± 6.00 | K | NIST |
Tboil | 519.95 ± 0.60 | K | NIST |
Tboil | 520.15 ± 2.00 | K | NIST |
Tboil | 518.95 ± 0.40 | K | NIST |
Tboil | 519.00 ± 5.00 | K | NIST |
Tboil | 520.35 ± 0.60 | K | NIST |
Tc | 787.00 | K | KDB |
Tfus | [270.30; 271.00] | K | |
Tfus | 271.00 | K | KDB |
Tfus | 270.30 ± 0.20 | K | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
ΔfusH | 12.52 | kJ/mol | 270.50 | NIST |
ΔvapH | [47.70; 61.20] | kJ/mol | [297.00; 482.00] | |
ΔvapH | 61.20 | kJ/mol | 297.00 | NIST |
ΔvapH | 61.00 ± 0.10 | kJ/mol | 436.00 | NIST |
ΔvapH | 55.60 ± 0.10 | kJ/mol | 436.00 | NIST |
ΔvapH | 53.00 ± 0.10 | kJ/mol | 436.00 | NIST |
ΔvapH | 50.40 ± 0.10 | kJ/mol | 436.00 | NIST |
ΔvapH | 47.70 ± 0.20 | kJ/mol | 436.00 | NIST |
ΔvapH | 58.20 ± 0.10 | kJ/mol | 436.00 | NIST |
ΔvapH | 54.70 | kJ/mol | 482.00 | NIST |
ρl | 1059.59 | kg/m3 | 293.10 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [383.53; 553.76] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45182e+01 | |||
Coefficient B | -4.43929e+03 | |||
Coefficient C | -7.15800e+01 | |||
Temperature range, min. | 383.53 | |||
Temperature range, max. | 553.76 | |||
Pvap | 1.33 | kPa | 383.53 | Calculated Property |
Pvap | 3.01 | kPa | 402.44 | Calculated Property |
Pvap | 6.21 | kPa | 421.36 | Calculated Property |
Pvap | 11.91 | kPa | 440.27 | Calculated Property |
Pvap | 21.44 | kPa | 459.19 | Calculated Property |
Pvap | 36.53 | kPa | 478.10 | Calculated Property |
Pvap | 59.35 | kPa | 497.02 | Calculated Property |
Pvap | 92.54 | kPa | 515.93 | Calculated Property |
Pvap | 139.15 | kPa | 534.85 | Calculated Property |
Pvap | 202.65 | kPa | 553.76 | Calculated Property |
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