Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -2461.00 | kJ/mol | NIST |
Cp,liquid | 236.63 | J/mol×K | Molar h... |
ΔfG° | -295.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -440.91 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | [-544.80; -541.80] | kJ/mol |
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ΔfH°liquid | -544.80 | kJ/mol | NIST |
ΔfH°liquid | -541.80 | kJ/mol | NIST |
ΔfusH° | 7.25 | kJ/mol | Joback Calculated Property |
ΔvapH° | 57.08 | kJ/mol | Joback Calculated Property |
log10WS | -0.25 | Crippen Calculated Property | |
logPoct/wat | -0.252 | Crippen Calculated Property | |
McVol | 78.960 | ml/mol | McGowan Calculated Property |
Pc | 5087.49 | kPa | Joback Calculated Property |
Inp | [746.00; 824.00] |
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|
Inp | 789.00 | NIST | |
Inp | 773.00 | NIST | |
Inp | Outlier 747.50 | NIST | |
Inp | 769.00 | NIST | |
Inp | 802.00 | NIST | |
Inp | 819.00 | NIST | |
Inp | 782.00 | NIST | |
Inp | 795.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 803.00 | NIST | |
Inp | 782.00 | NIST | |
Inp | Outlier 824.00 | NIST | |
Inp | 783.00 | NIST | |
Inp | 779.00 | NIST | |
Inp | 780.00 | NIST | |
Inp | 790.00 | NIST | |
Inp | 756.00 | NIST | |
Inp | 779.00 | NIST | |
Inp | 782.00 | NIST | |
Inp | 768.00 | NIST | |
Inp | Outlier 746.00 | NIST | |
Inp | Outlier 750.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 787.00 | NIST | |
Inp | 792.00 | NIST | |
Inp | 788.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 800.00 | NIST | |
Inp | 806.00 | NIST | |
Inp | 782.00 | NIST | |
Inp | 778.00 | NIST | |
Inp | 784.00 | NIST | |
Inp | 793.00 | NIST | |
Inp | 786.00 | NIST | |
Inp | 789.00 | NIST | |
Inp | 819.00 | NIST | |
Inp | 782.00 | NIST | |
I | [1492.00; 1590.00] |
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|
I | Outlier 1494.00 | NIST | |
I | Outlier 1492.00 | NIST | |
I | Outlier 1492.00 | NIST | |
I | 1522.00 | NIST | |
I | 1526.00 | NIST | |
I | 1580.00 | NIST | |
I | 1545.00 | NIST | |
I | 1570.00 | NIST | |
I | 1556.00 | NIST | |
I | 1542.00 | NIST | |
I | 1539.00 | NIST | |
I | 1543.00 | NIST | |
I | 1547.00 | NIST | |
I | 1543.00 | NIST | |
I | 1543.00 | NIST | |
I | 1541.00 | NIST | |
I | 1542.00 | NIST | |
I | 1583.00 | NIST | |
I | 1583.00 | NIST | |
I | 1579.00 | NIST | |
I | 1558.00 | NIST | |
I | 1562.00 | NIST | |
I | 1522.00 | NIST | |
I | 1541.00 | NIST | |
I | 1576.00 | NIST | |
I | 1554.00 | NIST | |
I | 1580.00 | NIST | |
I | 1542.00 | NIST | |
I | 1558.00 | NIST | |
I | 1523.00 | NIST | |
I | 1566.00 | NIST | |
I | 1539.00 | NIST | |
I | 1539.00 | NIST | |
I | 1526.00 | NIST | |
I | 1517.00 | NIST | |
I | 1512.00 | NIST | |
I | 1529.00 | NIST | |
I | 1536.00 | NIST | |
I | 1590.00 | NIST | |
I | 1563.00 | NIST | |
I | 1583.00 | NIST | |
I | 1553.00 | NIST | |
I | 1581.00 | NIST | |
I | 1524.00 | NIST | |
I | 1581.00 | NIST | |
I | 1550.00 | NIST | |
I | 1528.00 | NIST | |
I | 1577.00 | NIST | |
I | 1521.00 | NIST | |
I | 1583.00 | NIST | |
I | 1580.00 | NIST | |
I | 1539.00 | NIST | |
I | 1541.00 | NIST | |
I | 1558.00 | NIST | |
I | 1554.00 | NIST | |
I | 1566.00 | NIST | |
I | 1512.00 | NIST | |
I | Outlier 1494.00 | NIST | |
I | 1583.00 | NIST | |
Tboil | [415.15; 456.70] | K |
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Tboil | 454.21 | K | Vapor l... |
Tboil | 454.21 | K | Liquid ... |
Tboil | 454.21 | K | Liquid ... |
Tboil | 454.21 | K | Liquid ... |
Tboil | 456.70 | K | NIST |
Tboil | 455.65 ± 1.00 | K | NIST |
Tboil | 455.15 ± 4.00 | K | NIST |
Tboil | Outlier 415.15 ± 3.00 | K | NIST |
Tc | 639.26 | K | Joback Calculated Property |
Tfus | 292.15 ± 2.00 | K | NIST |
Vc | 0.285 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [173.55; 210.57] | J/mol×K | [474.40; 639.26] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 500 550 600 | ||||
Cp,gas | 173.55 | J/mol×K | 474.40 | Joback Calculated Property |
Cp,gas | 180.37 | J/mol×K | 501.88 | Joback Calculated Property |
Cp,gas | 186.92 | J/mol×K | 529.35 | Joback Calculated Property |
Cp,gas | 193.21 | J/mol×K | 556.83 | Joback Calculated Property |
Cp,gas | 199.24 | J/mol×K | 584.30 | Joback Calculated Property |
Cp,gas | 205.02 | J/mol×K | 611.78 | Joback Calculated Property |
Cp,gas | 210.57 | J/mol×K | 639.26 | Joback Calculated Property |
Cp,liquid | [213.00; 262.67] | J/mol×K | [298.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 210 220 230 240 250 260 300 320 340 | ||||
Cp,liquid | 236.67 | J/mol×K | 298.15 | Molar h... |
Cp,liquid | 213.00 | J/mol×K | 298.20 | NIST |
Cp,liquid | 239.28 | J/mol×K | 303.15 | Molar h... |
Cp,liquid | 241.85 | J/mol×K | 308.15 | Molar h... |
Cp,liquid | 244.35 | J/mol×K | 313.15 | Molar h... |
Cp,liquid | 246.82 | J/mol×K | 318.15 | Molar h... |
Cp,liquid | 249.23 | J/mol×K | 323.15 | Molar h... |
Cp,liquid | 251.60 | J/mol×K | 328.15 | Molar h... |
Cp,liquid | 253.91 | J/mol×K | 333.15 | Molar h... |
Cp,liquid | 256.17 | J/mol×K | 338.15 | Molar h... |
Cp,liquid | 258.39 | J/mol×K | 343.15 | Molar h... |
Cp,liquid | 260.55 | J/mol×K | 348.15 | Molar h... |
Cp,liquid | 262.67 | J/mol×K | 353.15 | Molar h... |
η | [0.0001208; 1.9625358] | Pa×s | [226.48; 474.40] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 0.5 1 1.5 2 300 400 | ||||
η | 1.9625358 | Pa×s | 226.48 | Joback Calculated Property |
η | 0.1120965 | Pa×s | 267.80 | Joback Calculated Property |
η | 0.0137635 | Pa×s | 309.12 | Joback Calculated Property |
η | 0.0027712 | Pa×s | 350.44 | Joback Calculated Property |
η | 0.0007824 | Pa×s | 391.76 | Joback Calculated Property |
η | 0.0002812 | Pa×s | 433.08 | Joback Calculated Property |
η | 0.0001208 | Pa×s | 474.40 | Joback Calculated Property |
ΔvapH | [55.70; 62.50] | kJ/mol | [378.00; 402.50] | ![]() |
ΔvapH | 57.90 | kJ/mol | 378.00 | NIST |
ΔvapH | 55.70 | kJ/mol | 379.50 | NIST |
ΔvapH | 58.40 | kJ/mol | 386.00 | NIST |
ΔvapH | 62.50 | kJ/mol | 402.50 | NIST |
n0 | 1.43660 | 298.15 | Densiti... | |
ρl | [990.72; 990.72] | kg/m3 | [308.15; 308.15] | ![]() |
ρl | 990.72 | kg/m3 | 308.15 | Effect ... |
ρl | 990.72 | kg/m3 | 308.15 | A compa... |
ρl | 990.72 | kg/m3 | 308.15 | Thermod... |
ρl | 990.72 | kg/m3 | 308.15 | Effect ... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [351.12; 481.36] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.62445e+01 | |||
Coefficient B | -4.52281e+03 | |||
Coefficient C | -6.76820e+01 | |||
Temperature range, min. | 351.12 | |||
Temperature range, max. | 481.36 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 351.12 | Calculated Property |
Pvap | 2.89 | kPa | 365.59 | Calculated Property |
Pvap | 5.85 | kPa | 380.06 | Calculated Property |
Pvap | 11.10 | kPa | 394.53 | Calculated Property |
Pvap | 19.96 | kPa | 409.00 | Calculated Property |
Pvap | 34.21 | kPa | 423.48 | Calculated Property |
Pvap | 56.23 | kPa | 437.95 | Calculated Property |
Pvap | 89.02 | kPa | 452.42 | Calculated Property |
Pvap | 136.33 | kPa | 466.89 | Calculated Property |
Pvap | 202.63 | kPa | 481.36 | Calculated Property |
Pvap | [5.07e-03; 5358.29] | kPa | [280.75; 611.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.37891e+02 | |||
Coefficient B | -1.22864e+04 | |||
Coefficient C | -1.78282e+01 | |||
Coefficient D | 1.38579e-05 | |||
Temperature range, min. | 280.75 | |||
Temperature range, max. | 611.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 600 | ||||
Pvap | 5.07e-03 | kPa | 280.75 | Calculated Property |
Pvap | 0.12 | kPa | 317.44 | Calculated Property |
Pvap | 1.34 | kPa | 354.14 | Calculated Property |
Pvap | 8.74 | kPa | 390.83 | Calculated Property |
Pvap | 39.74 | kPa | 427.53 | Calculated Property |
Pvap | 139.69 | kPa | 464.22 | Calculated Property |
Pvap | 408.58 | kPa | 500.92 | Calculated Property |
Pvap | 1047.90 | kPa | 537.61 | Calculated Property |
Pvap | 2448.03 | kPa | 574.31 | Calculated Property |
Pvap | 5358.29 | kPa | 611.00 | Calculated Property |
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