Property | Value | Unit | Source |
---|---|---|---|
ω | 1.0060 | KDB | |
ΔcH°solid | [-9213.00; -9167.00] | kJ/mol |
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ΔcH°solid | -9168.40 ± 1.20 | kJ/mol | NIST |
ΔcH°solid | -9213.00 ± 8.00 | kJ/mol | NIST |
ΔcH°solid | -9167.00 ± 0.60 | kJ/mol | NIST |
ΔfG° | -69.82 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-476.20; -474.80] | kJ/mol |
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ΔfH°gas | -474.80 ± 2.60 | kJ/mol | NIST |
ΔfH°gas | -476.20 | kJ/mol | NIST |
ΔfH°solid | [-629.60; -628.20] | kJ/mol |
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ΔfH°solid | -628.20 ± 1.50 | kJ/mol | NIST |
ΔfH°solid | -629.60 ± 0.60 | kJ/mol | NIST |
ΔfusH° | [47.60; 98.90] | kJ/mol |
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ΔfusH° | 47.60 | kJ/mol | Solid-L... |
ΔfusH° | 98.90 | kJ/mol | Evaluat... |
ΔsubH° | [102.20; 153.40] | kJ/mol |
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ΔsubH° | 153.40 ± 1.90 | kJ/mol | NIST |
ΔsubH° | 153.40 | kJ/mol | NIST |
ΔsubH° | 102.20 ± 2.30 | kJ/mol | NIST |
ΔsubH° | 144.00 ± 2.00 | kJ/mol | NIST |
ΔvapH° | [98.70; 102.20] | kJ/mol |
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ΔvapH° | 102.20 | kJ/mol | NIST |
ΔvapH° | 98.90 ± 2.50 | kJ/mol | NIST |
ΔvapH° | 98.70 | kJ/mol | NIST |
ΔvapH° | 102.20 ± 2.30 | kJ/mol | NIST |
log10WS | [-6.11; -5.84] |
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|
log10WS | -5.84 | Estimat... | |
log10WS | -6.11 | Aq. Sol... | |
logPoct/wat | 4.680 | Crippen Calculated Property | |
McVol | 213.990 | ml/mol | McGowan Calculated Property |
Pc | 1810.00 | kPa | KDB |
Inp | [282.29; 1692.00] |
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|
Inp | 1675.00 | NIST | |
Inp | 1664.40 | NIST | |
Inp | 1678.20 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1669.00 | NIST | |
Inp | 1646.00 | NIST | |
Inp | 1652.00 | NIST | |
Inp | 1655.00 | NIST | |
Inp | 1657.00 | NIST | |
Inp | 1659.00 | NIST | |
Inp | 1653.00 | NIST | |
Inp | 1661.00 | NIST | |
Inp | 1670.00 | NIST | |
Inp | 1658.00 | NIST | |
Inp | 1669.00 | NIST | |
Inp | 1664.00 | NIST | |
Inp | 1680.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1680.00 | NIST | |
Inp | 1673.00 | NIST | |
Inp | 1679.00 | NIST | |
Inp | 1674.00 | NIST | |
Inp | 1686.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1672.00 | NIST | |
Inp | 1661.00 | NIST | |
Inp | 1647.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1679.00 | NIST | |
Inp | 1681.10 | NIST | |
Inp | 1664.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1647.00 | NIST | |
Inp | 1647.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1670.00 | NIST | |
Inp | 1687.00 | NIST | |
Inp | 1680.60 | NIST | |
Inp | 1660.00 | NIST | |
Inp | 1665.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1680.00 | NIST | |
Inp | 1677.00 | NIST | |
Inp | 1668.00 | NIST | |
Inp | 1652.00 | NIST | |
Inp | 1659.00 | NIST | |
Inp | 1663.00 | NIST | |
Inp | 1665.00 | NIST | |
Inp | 1653.00 | NIST | |
Inp | 1678.00 | NIST | |
Inp | 1685.00 | NIST | |
Inp | 1671.00 | NIST | |
Inp | 1683.00 | NIST | |
Inp | 1692.00 | NIST | |
Inp | 1692.00 | NIST | |
Inp | 1672.00 | NIST | |
Inp | 1684.00 | NIST | |
Inp | 1680.00 | NIST | |
Inp | 1672.00 | NIST | |
Inp | 1673.00 | NIST | |
Inp | 1677.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1680.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1677.00 | NIST | |
Inp | 1673.00 | NIST | |
Inp | 1662.00 | NIST | |
Inp | 1665.00 | NIST | |
Inp | Outlier 282.29 | NIST | |
Inp | Outlier 283.90 | NIST | |
Inp | Outlier 283.29 | NIST | |
Inp | 1679.00 | NIST | |
Inp | 1675.00 | NIST | |
Inp | 1685.00 | NIST | |
Inp | 1672.00 | NIST | |
Inp | 1677.00 | NIST | |
Inp | 1673.00 | NIST | |
Inp | 1676.00 | NIST | |
Inp | 1660.00 | NIST | |
Inp | 1668.00 | NIST | |
Inp | 1653.00 | NIST | |
I | [2123.00; 2204.00] |
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|
I | 2137.00 | NIST | |
I | 2175.00 | NIST | |
I | 2164.00 | NIST | |
I | 2161.00 | NIST | |
I | 2165.00 | NIST | |
I | 2165.00 | NIST | |
I | 2177.00 | NIST | |
I | 2170.00 | NIST | |
I | 2200.00 | NIST | |
I | Outlier 2123.00 | NIST | |
I | 2174.00 | NIST | |
I | 2155.00 | NIST | |
I | Outlier 2204.00 | NIST | |
I | 2173.00 | NIST | |
I | 2157.00 | NIST | |
I | 2157.00 | NIST | |
I | 2131.00 | NIST | |
I | 2152.00 | NIST | |
I | 2145.00 | NIST | |
I | 2180.00 | NIST | |
I | 2169.00 | NIST | |
I | 2179.00 | NIST | |
I | 2179.00 | NIST | |
I | 2152.00 | NIST | |
I | 2172.00 | NIST | |
I | 2175.00 | NIST | |
I | 2157.00 | NIST | |
I | 2179.00 | NIST | |
I | 2157.00 | NIST | |
Tboil | [562.00; 562.20] | K |
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Tboil | 562.00 | K | KDB |
Tboil | 562.20 | K | NIST |
Tc | 747.00 | K | KDB |
Tfus | [309.15; 312.65] | K |
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Tfus | 312.60 | K | KDB |
Tfus | 312.65 | K | Aq. Sol... |
Tfus | 310.71 | K | Solid-l... |
Tfus | 309.15 | K | The man... |
Tfus | 310.60 | K | High Pr... |
Tfus | 311.00 ± 1.00 | K | NIST |
Tfus | 310.15 ± 0.50 | K | NIST |
Tfus | 311.00 ± 0.05 | K | NIST |
Tfus | 311.21 ± 0.05 | K | NIST |
Tfus | 310.79 ± 0.50 | K | NIST |
Tfus | 310.10 ± 0.60 | K | NIST |
Tfus | 310.20 ± 2.00 | K | NIST |
Tfus | 312.00 ± 1.20 | K | NIST |
Tfus | 309.55 ± 0.50 | K | NIST |
Tfus | 310.75 ± 0.20 | K | NIST |
Tfus | 311.00 ± 1.50 | K | NIST |
Ttriple | 311.35 ± 0.50 | K | NIST |
Vc | 0.839 | m3/kmol | KDB |
Zc | 0.2443570 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [582.64; 668.61] | J/mol×K | [611.90; 769.95] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 580 600 620 640 660 650 700 750 | ||||
Cp,gas | 582.64 | J/mol×K | 611.90 | Joback Calculated Property |
Cp,gas | 598.48 | J/mol×K | 638.24 | Joback Calculated Property |
Cp,gas | 613.68 | J/mol×K | 664.58 | Joback Calculated Property |
Cp,gas | 628.28 | J/mol×K | 690.93 | Joback Calculated Property |
Cp,gas | 642.29 | J/mol×K | 717.27 | Joback Calculated Property |
Cp,gas | 655.72 | J/mol×K | 743.61 | Joback Calculated Property |
Cp,gas | 668.61 | J/mol×K | 769.95 | Joback Calculated Property |
Cp,liquid | 516.00 | J/mol×K | 313.15 | NIST |
Cp,solid | [388.00; 506.00] | J/mol×K | [298.15; 312.00] | ![]() |
Cp,solid | 426.50 | J/mol×K | 298.15 | NIST |
Cp,solid | 388.00 | J/mol×K | 298.15 | NIST |
Cp,solid | 506.00 | J/mol×K | 312.00 | NIST |
η | [0.0000598; 0.0130512] | Pa×s | [308.36; 611.90] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 0.01 0.01 400 500 600 | ||||
η | 0.0130512 | Pa×s | 308.36 | Joback Calculated Property |
η | 0.0028250 | Pa×s | 358.95 | Joback Calculated Property |
η | 0.0008925 | Pa×s | 409.54 | Joback Calculated Property |
η | 0.0003633 | Pa×s | 460.13 | Joback Calculated Property |
η | 0.0001767 | Pa×s | 510.72 | Joback Calculated Property |
η | 0.0000978 | Pa×s | 561.31 | Joback Calculated Property |
η | 0.0000598 | Pa×s | 611.90 | Joback Calculated Property |
ΔfusH | [1.80; 49.40] | kJ/mol | [306.00; 311.60] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 10 20 30 40 50 306 308 310 | ||||
ΔfusH | 1.80 | kJ/mol | 306.00 | NIST |
ΔfusH | 47.29 | kJ/mol | 308.10 | NIST |
ΔfusH | 25.10 | kJ/mol | 310.80 | NIST |
ΔfusH | 49.40 | kJ/mol | 311.00 | NIST |
ΔfusH | 23.81 | kJ/mol | 311.00 | NIST |
ΔfusH | 49.37 | kJ/mol | 311.00 | NIST |
ΔfusH | 47.01 | kJ/mol | 311.20 | NIST |
ΔfusH | 22.01 | kJ/mol | 311.60 | NIST |
ΔsubH | 143.90 | kJ/mol | 300.00 | NIST |
ΔvapH | [72.17; 109.00] | kJ/mol | [319.50; 536.40] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 70 80 90 100 110 350 400 450 500 | ||||
ΔvapH | 104.20 | kJ/mol | 319.50 | NIST |
ΔvapH | 93.60 | kJ/mol | 329.00 | NIST |
ΔvapH | 106.40 | kJ/mol | 335.50 | NIST |
ΔvapH | 109.00 | kJ/mol | 337.50 | NIST |
ΔvapH | 81.80 | kJ/mol | 385.50 | NIST |
ΔvapH | 76.60 | kJ/mol | 496.50 | NIST |
ΔvapH | 72.17 | kJ/mol | 536.40 | KDB |
Pvap | [8.32; 29.35] | kPa | [479.42; 519.18] | ![]() |
T(K) Vapor pressure (kPa) 10 15 20 25 30 480 500 520 | ||||
Pvap | 8.32 | kPa | 479.42 | Vapor p... |
Pvap | 11.05 | kPa | 487.56 | Vapor p... |
Pvap | 11.05 | kPa | 487.56 | Vapor p... |
Pvap | 13.89 | kPa | 494.50 | Vapor p... |
Pvap | 16.78 | kPa | 500.44 | Vapor p... |
Pvap | 20.26 | kPa | 506.63 | Vapor p... |
Pvap | 24.53 | kPa | 513.01 | Vapor p... |
Pvap | 24.53 | kPa | 513.07 | Vapor p... |
Pvap | 29.35 | kPa | 519.11 | Vapor p... |
Pvap | 29.35 | kPa | 519.18 | Vapor p... |
ΔfusS | [5.86; 158.75] | J/mol×K | [306.00; 311.60] | ![]() |
T(K) Entropy of fusion at a given temperature (J/mol×K) 0 20 40 60 80 100 120 140 160 306 308 310 | ||||
ΔfusS | 5.86 | J/mol×K | 306.00 | NIST |
ΔfusS | 80.75 | J/mol×K | 310.80 | NIST |
ΔfusS | 76.57 | J/mol×K | 311.00 | NIST |
ΔfusS | 158.75 | J/mol×K | 311.00 | NIST |
ΔfusS | 151.04 | J/mol×K | 311.20 | NIST |
ΔfusS | 70.71 | J/mol×K | 311.60 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [442.04; 589.72] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.69720e+01 | |||
Coefficient B | -5.71881e+03 | |||
Coefficient C | -9.92760e+01 | |||
Temperature range, min. | 442.04 | |||
Temperature range, max. | 589.72 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 450 500 550 | ||||
Pvap | 1.33 | kPa | 442.04 | Calculated Property |
Pvap | 2.86 | kPa | 458.45 | Calculated Property |
Pvap | 5.73 | kPa | 474.86 | Calculated Property |
Pvap | 10.84 | kPa | 491.27 | Calculated Property |
Pvap | 19.47 | kPa | 507.68 | Calculated Property |
Pvap | 33.45 | kPa | 524.08 | Calculated Property |
Pvap | 55.18 | kPa | 540.49 | Calculated Property |
Pvap | 87.82 | kPa | 556.90 | Calculated Property |
Pvap | 135.36 | kPa | 573.31 | Calculated Property |
Pvap | 202.66 | kPa | 589.72 | Calculated Property |
Pvap | [8.63e-05; 1801.78] | kPa | [310.65; 741.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 2.83615e+02 | |||
Coefficient B | -2.31007e+04 | |||
Coefficient C | -3.83547e+01 | |||
Coefficient D | 1.54882e-05 | |||
Temperature range, min. | 310.65 | |||
Temperature range, max. | 741.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 400 500 600 700 | ||||
Pvap | 8.63e-05 | kPa | 310.65 | Calculated Property |
Pvap | 0.01 | kPa | 358.47 | Calculated Property |
Pvap | 0.34 | kPa | 406.28 | Calculated Property |
Pvap | 3.57 | kPa | 454.10 | Calculated Property |
Pvap | 19.80 | kPa | 501.92 | Calculated Property |
Pvap | 72.08 | kPa | 549.73 | Calculated Property |
Pvap | 198.56 | kPa | 597.55 | Calculated Property |
Pvap | 456.38 | kPa | 645.37 | Calculated Property |
Pvap | 936.72 | kPa | 693.18 | Calculated Property |
Pvap | 1801.78 | kPa | 741.00 | Calculated Property |
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