Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -7486.50 ± 1.30 | kJ/mol | NIST |
ΔfG° | -183.76 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -535.81 | kJ/mol | Joback Calculated Property |
ΔfusH° | 36.20 | kJ/mol | Heat Ca... |
ΔvapH° | [70.60; 72.40] | kJ/mol |
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ΔvapH° | 70.80 ± 0.40 | kJ/mol | NIST |
ΔvapH° | 70.60 | kJ/mol | NIST |
ΔvapH° | 71.37 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 71.40 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 72.40 | kJ/mol | NIST |
log10WS | -3.71 | Crippen Calculated Property | |
logPoct/wat | 3.690 | Crippen Calculated Property | |
McVol | 187.380 | ml/mol | McGowan Calculated Property |
Pc | 1851.52 | kPa | Joback Calculated Property |
Inp | [1405.00; 1432.00] |
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|
Inp | 1411.00 | NIST | |
Inp | 1422.00 | NIST | |
Inp | 1407.00 | NIST | |
Inp | 1406.00 | NIST | |
Inp | 1419.00 | NIST | |
Inp | 1420.00 | NIST | |
Inp | 1427.00 | NIST | |
Inp | 1410.00 | NIST | |
Inp | 1421.50 | NIST | |
Inp | 1422.50 | NIST | |
Inp | 1410.00 | NIST | |
Inp | 1407.00 | NIST | |
Inp | 1407.00 | NIST | |
Inp | 1432.00 | NIST | |
Inp | 1427.00 | NIST | |
Inp | 1430.00 | NIST | |
Inp | 1405.00 | NIST | |
Inp | 1405.00 | NIST | |
Inp | 1429.00 | NIST | |
Inp | 1429.00 | NIST | |
Inp | 1406.00 | NIST | |
Inp | 1414.00 | NIST | |
Inp | 1408.00 | NIST | |
Inp | 1410.00 | NIST | |
Inp | 1407.00 | NIST | |
Inp | 1405.00 | NIST | |
Inp | 1419.00 | NIST | |
I | [1665.00; 1732.00] |
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|
I | 1699.00 | NIST | |
I | 1732.00 | NIST | |
I | 1672.00 | NIST | |
I | 1696.60 | NIST | |
I | 1704.60 | NIST | |
I | 1705.70 | NIST | |
I | 1728.70 | NIST | |
I | 1686.70 | NIST | |
I | 1701.80 | NIST | |
I | 1706.60 | NIST | |
I | 1711.60 | NIST | |
I | 1710.00 | NIST | |
I | 1732.00 | NIST | |
I | 1694.00 | NIST | |
I | 1703.00 | NIST | |
I | 1710.00 | NIST | |
I | Outlier 1665.00 | NIST | |
I | 1695.00 | NIST | |
Tboil | 344.15 ± 2.00 | K | NIST |
Tc | 720.05 | K | Joback Calculated Property |
Tfus | 261.80 ± 0.05 | K | NIST |
Ttriple | 262.00 | K | Heat ca... |
Vc | 0.732 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [464.17; 549.22] | J/mol×K | [550.25; 720.05] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 460 480 500 520 540 550 600 650 700 | ||||
Cp,gas | 464.17 | J/mol×K | 550.25 | Joback Calculated Property |
Cp,gas | 479.84 | J/mol×K | 578.55 | Joback Calculated Property |
Cp,gas | 494.90 | J/mol×K | 606.85 | Joback Calculated Property |
Cp,gas | 509.36 | J/mol×K | 635.15 | Joback Calculated Property |
Cp,gas | 523.23 | J/mol×K | 663.45 | Joback Calculated Property |
Cp,gas | 536.51 | J/mol×K | 691.75 | Joback Calculated Property |
Cp,gas | 549.22 | J/mol×K | 720.05 | Joback Calculated Property |
Cp,liquid | [411.40; 446.50] | J/mol×K | [303.15; 373.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 410 420 430 440 450 320 340 360 | ||||
Cp,liquid | 411.40 | J/mol×K | 303.15 | Heat ca... |
Cp,liquid | 415.90 | J/mol×K | 313.15 | Heat ca... |
Cp,liquid | 420.90 | J/mol×K | 323.15 | Heat ca... |
Cp,liquid | 426.10 | J/mol×K | 333.15 | Heat ca... |
Cp,liquid | 431.40 | J/mol×K | 343.15 | Heat ca... |
Cp,liquid | 436.70 | J/mol×K | 353.15 | Heat ca... |
Cp,liquid | 441.80 | J/mol×K | 363.15 | Heat ca... |
Cp,liquid | 446.50 | J/mol×K | 373.15 | Heat ca... |
η | [0.0001878; 0.0030867] | Pa×s | [297.16; 550.25] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 300 400 500 | ||||
η | 0.0030867 | Pa×s | 297.16 | Joback Calculated Property |
η | 0.0014485 | Pa×s | 339.34 | Joback Calculated Property |
η | 0.0008035 | Pa×s | 381.52 | Joback Calculated Property |
η | 0.0005012 | Pa×s | 423.70 | Joback Calculated Property |
η | 0.0003406 | Pa×s | 465.89 | Joback Calculated Property |
η | 0.0002467 | Pa×s | 508.07 | Joback Calculated Property |
η | 0.0001878 | Pa×s | 550.25 | Joback Calculated Property |
ΔvapH | [60.90; 67.00] | kJ/mol | [340.00; 433.00] | ![]() |
ΔvapH | 67.00 ± 0.10 | kJ/mol | 340.00 | NIST |
ΔvapH | 66.10 | kJ/mol | 350.00 | NIST |
ΔvapH | 60.90 | kJ/mol | 433.00 | NIST |
Pvap | [3.58e-03; 0.01] | kPa | [305.25; 317.52] | ![]() |
T(K) Vapor pressure (kPa) 4.00e-3 6.00e-3 8.00e-3 0.01 305 310 315 | ||||
Pvap | 3.58e-03 | kPa | 305.25 | Fatty a... |
Pvap | 4.50e-03 | kPa | 307.81 | Fatty a... |
Pvap | 5.57e-03 | kPa | 310.15 | Fatty a... |
Pvap | 6.96e-03 | kPa | 312.67 | Fatty a... |
Pvap | 8.55e-03 | kPa | 315.06 | Fatty a... |
Pvap | 0.01 | kPa | 317.52 | Fatty a... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [389.72; 540.23] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.55084e+01 | |||
Coefficient B | -4.64990e+03 | |||
Coefficient C | -8.42230e+01 | |||
Temperature range, min. | 389.72 | |||
Temperature range, max. | 540.23 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 389.72 | Calculated Property |
Pvap | 2.94 | kPa | 406.44 | Calculated Property |
Pvap | 5.99 | kPa | 423.17 | Calculated Property |
Pvap | 11.41 | kPa | 439.89 | Calculated Property |
Pvap | 20.53 | kPa | 456.61 | Calculated Property |
Pvap | 35.11 | kPa | 473.34 | Calculated Property |
Pvap | 57.44 | kPa | 490.06 | Calculated Property |
Pvap | 90.40 | kPa | 506.78 | Calculated Property |
Pvap | 137.44 | kPa | 523.51 | Calculated Property |
Pvap | 202.63 | kPa | 540.23 | Calculated Property |
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