Property | Value | Unit | Source |
---|---|---|---|
Cp,liquid | 356.31 | J/mol×K | Vapour ... |
ΔfG° | -114.36 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -386.60 | kJ/mol | Joback Calculated Property |
ΔfusH° | 19.63 | kJ/mol | Joback Calculated Property |
ΔvapH° | 72.90 ± 0.60 | kJ/mol | NIST |
log10WS | [-2.74; -2.74] |
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|
log10WS | -2.74 | Aq. Sol... | |
log10WS | -2.74 | Estimat... | |
logPoct/wat | 2.728 | Crippen Calculated Property | |
McVol | 143.540 | ml/mol | McGowan Calculated Property |
Pc | [2530.00; 2530.00] | kPa |
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Pc | 2530.00 | kPa | KDB |
Pc | 2530.00 ± 50.00 | kPa | NIST |
Pc | 2530.00 ± 20.00 | kPa | NIST |
Pc | 2530.00 ± 20.00 | kPa | NIST |
ρc | [251.00; 251.00] | kg/m3 |
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ρc | 251.00 ± 7.21 | kg/m3 | NIST |
ρc | 251.00 ± 5.77 | kg/m3 | NIST |
Inp | [1072.00; 1120.00] |
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|
Inp | 1091.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1108.70 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1085.00 | NIST | |
Inp | 1085.00 | NIST | |
Inp | 1085.00 | NIST | |
Inp | 1102.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1101.00 | NIST | |
Inp | 1097.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1100.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1076.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | Outlier 1072.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1106.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1110.00 | NIST | |
Inp | Outlier 1120.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1091.00 | NIST | |
Inp | 1089.00 | NIST | |
Inp | 1084.00 | NIST | |
Inp | Outlier 1120.00 | NIST | |
Inp | 1098.00 | NIST | |
Inp | 1087.00 | NIST | |
Inp | 1092.00 | NIST | |
Inp | 1085.00 | NIST | |
Inp | 1103.00 | NIST | |
Inp | 1089.00 | NIST | |
I | [1483.00; 1547.00] |
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|
I | 1488.00 | NIST | |
I | 1489.00 | NIST | |
I | 1508.00 | NIST | |
I | 1511.00 | NIST | |
I | 1547.00 | NIST | |
I | 1524.00 | NIST | |
I | 1528.00 | NIST | |
I | 1521.00 | NIST | |
I | 1545.00 | NIST | |
I | 1532.00 | NIST | |
I | 1505.00 | NIST | |
I | 1533.00 | NIST | |
I | 1534.00 | NIST | |
I | 1532.00 | NIST | |
I | 1514.00 | NIST | |
I | Outlier 1483.00 | NIST | |
I | 1520.00 | NIST | |
I | 1521.00 | NIST | |
I | 1524.00 | NIST | |
I | 1485.00 | NIST | |
I | 1528.00 | NIST | |
I | 1528.00 | NIST | |
I | 1509.00 | NIST | |
I | 1535.00 | NIST | |
I | 1515.00 | NIST | |
I | 1535.00 | NIST | |
I | 1535.00 | NIST | |
I | 1535.00 | NIST | |
I | 1537.00 | NIST | |
I | 1508.00 | NIST | |
I | 1530.00 | NIST | |
I | 1510.00 | NIST | |
I | 1499.00 | NIST | |
I | 1525.00 | NIST | |
I | 1518.00 | NIST | |
I | 1538.00 | NIST | |
I | 1522.00 | NIST | |
I | 1530.00 | NIST | |
I | Outlier 1484.00 | NIST | |
I | 1519.00 | NIST | |
I | 1490.00 | NIST | |
I | 1528.00 | NIST | |
I | 1528.00 | NIST | |
I | 1522.00 | NIST | |
I | 1516.00 | NIST | |
I | 1521.00 | NIST | |
I | 1499.00 | NIST | |
I | 1518.00 | NIST | |
I | 1521.00 | NIST | |
I | Outlier 1484.00 | NIST | |
I | 1521.00 | NIST | |
I | 1509.00 | NIST | |
I | 1488.00 | NIST | |
I | 1508.00 | NIST | |
I | 1518.00 | NIST | |
I | 1519.00 | NIST | |
I | 1528.00 | NIST | |
I | 1499.00 | NIST | |
I | 1509.00 | NIST | |
Tboil | [465.65; 473.15] | K |
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Tboil | 466.70 | K | NIST |
Tboil | 473.15 ± 5.00 | K | NIST |
Tboil | 471.50 ± 0.60 | K | NIST |
Tboil | 471.35 ± 1.00 | K | NIST |
Tboil | 466.15 ± 3.00 | K | NIST |
Tboil | 465.65 ± 5.00 | K | NIST |
Tboil | 468.65 ± 3.00 | K | NIST |
Tboil | 470.65 ± 3.00 | K | NIST |
Tboil | 466.65 ± 3.00 | K | NIST |
Tboil | 466.65 ± 5.00 | K | NIST |
Tboil | 466.65 ± 3.00 | K | NIST |
Tc | [649.10; 650.10] | K |
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Tc | 649.60 | K | KDB |
Tc | 650.00 ± 1.00 | K | NIST |
Tc | 650.10 ± 0.60 | K | NIST |
Tc | 650.10 ± 0.60 | K | NIST |
Tc | 649.50 | K | NIST |
Tc | 649.10 ± 0.30 | K | NIST |
Tfus | 237.98 | K | Aq. Sol... |
Vc | [0.575; 0.575] | m3/kmol |
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Vc | 0.575 | m3/kmol | KDB |
Vc | 0.575 | m3/kmol | NIST |
Zc | 0.2693430 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [334.58; 403.87] | J/mol×K | [497.06; 659.14] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 340 360 380 400 500 550 600 650 | ||||
Cp,gas | 334.58 | J/mol×K | 497.06 | Joback Calculated Property |
Cp,gas | 347.30 | J/mol×K | 524.07 | Joback Calculated Property |
Cp,gas | 359.54 | J/mol×K | 551.09 | Joback Calculated Property |
Cp,gas | 371.30 | J/mol×K | 578.10 | Joback Calculated Property |
Cp,gas | 382.60 | J/mol×K | 605.11 | Joback Calculated Property |
Cp,gas | 393.45 | J/mol×K | 632.13 | Joback Calculated Property |
Cp,gas | 403.87 | J/mol×K | 659.14 | Joback Calculated Property |
η | [0.0001409; 0.0878509] | Pa×s | [237.01; 497.06] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 0.02 0.04 0.06 0.08 300 400 500 | ||||
η | 0.0878509 | Pa×s | 237.01 | Joback Calculated Property |
η | 0.0131188 | Pa×s | 280.35 | Joback Calculated Property |
η | 0.0032599 | Pa×s | 323.69 | Joback Calculated Property |
η | 0.0011254 | Pa×s | 367.03 | Joback Calculated Property |
η | 0.0004864 | Pa×s | 410.38 | Joback Calculated Property |
η | 0.0002468 | Pa×s | 453.72 | Joback Calculated Property |
η | 0.0001409 | Pa×s | 497.06 | Joback Calculated Property |
ΔvapH | [55.50; 79.60] | kJ/mol | [303.00; 417.50] | ![]() |
ΔvapH | 79.60 | kJ/mol | 303.00 | NIST |
ΔvapH | 55.50 | kJ/mol | 417.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [364.09; 493.39] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.64188e+01 | |||
Coefficient B | -4.61124e+03 | |||
Coefficient C | -7.82320e+01 | |||
Temperature range, min. | 364.09 | |||
Temperature range, max. | 493.39 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 | ||||
Pvap | 1.33 | kPa | 364.09 | Calculated Property |
Pvap | 2.88 | kPa | 378.46 | Calculated Property |
Pvap | 5.82 | kPa | 392.82 | Calculated Property |
Pvap | 11.03 | kPa | 407.19 | Calculated Property |
Pvap | 19.84 | kPa | 421.56 | Calculated Property |
Pvap | 34.02 | kPa | 435.92 | Calculated Property |
Pvap | 55.97 | kPa | 450.29 | Calculated Property |
Pvap | 88.74 | kPa | 464.66 | Calculated Property |
Pvap | 136.11 | kPa | 479.02 | Calculated Property |
Pvap | 202.67 | kPa | 493.39 | Calculated Property |
Pvap | [5.24e-06; 2379.40] | kPa | [238.51; 623.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.35307e+02 | |||
Coefficient B | -1.31543e+04 | |||
Coefficient C | -1.69302e+01 | |||
Coefficient D | 6.49313e-06 | |||
Temperature range, min. | 238.51 | |||
Temperature range, max. | 623.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 300 400 500 600 | ||||
Pvap | 5.24e-06 | kPa | 238.51 | Calculated Property |
Pvap | 1.62e-03 | kPa | 281.23 | Calculated Property |
Pvap | 0.08 | kPa | 323.95 | Calculated Property |
Pvap | 1.41 | kPa | 366.67 | Calculated Property |
Pvap | 11.41 | kPa | 409.39 | Calculated Property |
Pvap | 56.21 | kPa | 452.12 | Calculated Property |
Pvap | 195.40 | kPa | 494.84 | Calculated Property |
Pvap | 529.58 | kPa | 537.56 | Calculated Property |
Pvap | 1198.74 | kPa | 580.28 | Calculated Property |
Pvap | 2379.40 | kPa | 623.00 | Calculated Property |
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