Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2660 | KDB | |
PAff | 826.30 | kJ/mol | NIST |
BasG | 797.10 | kJ/mol | NIST |
ΔcH°gas | -2751.10 ± 0.92 | kJ/mol | NIST |
ΔfG° | -121.00 | kJ/mol | KDB |
ΔfH°gas | [-252.20; -252.00] | kJ/mol |
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ΔfH°gas | -252.20 | kJ/mol | KDB |
ΔfH°gas | -252.00 ± 0.96 | kJ/mol | NIST |
ΔfusH° | 3.78 | kJ/mol | Joback Calculated Property |
ΔvapH° | [26.40; 26.78] | kJ/mol |
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ΔvapH° | 26.78 | kJ/mol | NIST |
ΔvapH° | 26.41 | kJ/mol | NIST |
ΔvapH° | 26.40 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 26.40 | kJ/mol | NIST |
IE | [9.42; 9.50] | eV |
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IE | 9.45 ± 0.04 | eV | NIST |
IE | 9.50 | eV | NIST |
IE | 9.42 ± 0.07 | eV | NIST |
IE | 9.42 | eV | NIST |
log10WS | -0.06 | Aq. Sol... | |
logPoct/wat | 1.041 | Crippen Calculated Property | |
McVol | 73.090 | ml/mol | McGowan Calculated Property |
Pc | [3762.00; 3762.00] | kPa |
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Pc | 3762.00 | kPa | KDB |
Pc | 3762.00 ± 4.00 | kPa | NIST |
S°gas | 341.60 | J/mol×K | NIST |
S°liquid | 253.70 | J/mol×K | NIST |
Tboil | [303.90; 303.92] | K |
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Tboil | 303.92 | K | KDB |
Tboil | 303.90 | K | NIST |
Tc | [464.48; 464.50] | K |
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Tc | 464.48 | K | KDB |
Tc | 464.50 | K | NIST |
Tc | 464.48 ± 0.20 | K | NIST |
Tfus | 142.07 | K | Joback Calculated Property |
Ttriple | [123.06; 127.93] | K |
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Ttriple | 127.93 ± 0.05 | K | NIST |
Ttriple | 127.93 ± 0.05 | K | NIST |
Ttriple | 123.06 ± 0.10 | K | NIST |
Vc | 0.272 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [116.25; 158.04] | J/mol×K | [312.90; 480.53] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 120 130 140 150 160 350 400 450 | ||||
Cp,gas | 116.25 | J/mol×K | 312.90 | Joback Calculated Property |
Cp,gas | 123.64 | J/mol×K | 340.84 | Joback Calculated Property |
Cp,gas | 130.85 | J/mol×K | 368.78 | Joback Calculated Property |
Cp,gas | 137.91 | J/mol×K | 396.71 | Joback Calculated Property |
Cp,gas | 144.79 | J/mol×K | 424.65 | Joback Calculated Property |
Cp,gas | 151.50 | J/mol×K | 452.59 | Joback Calculated Property |
Cp,gas | 158.04 | J/mol×K | 480.53 | Joback Calculated Property |
Cp,liquid | 161.90 | J/mol×K | 298.15 | NIST |
η | [0.0001944; 0.0050393] | Pa×s | [142.07; 312.90] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 150 200 250 300 | ||||
η | 0.0050393 | Pa×s | 142.07 | Joback Calculated Property |
η | 0.0018626 | Pa×s | 170.54 | Joback Calculated Property |
η | 0.0009152 | Pa×s | 199.01 | Joback Calculated Property |
η | 0.0005373 | Pa×s | 227.48 | Joback Calculated Property |
η | 0.0003551 | Pa×s | 255.96 | Joback Calculated Property |
η | 0.0002550 | Pa×s | 284.43 | Joback Calculated Property |
η | 0.0001944 | Pa×s | 312.90 | Joback Calculated Property |
ΔfusH | [5.85; 5.85] | kJ/mol | [127.30; 127.30] | ![]() |
ΔfusH | 5.85 | kJ/mol | 127.30 | NIST |
ΔfusH | 5.85 | kJ/mol | 127.30 | NIST |
ΔvapH | [26.05; 28.80] | kJ/mol | [287.50; 303.90] | ![]() |
ΔvapH | 28.80 | kJ/mol | 287.50 | NIST |
ΔvapH | 28.40 | kJ/mol | 292.50 | NIST |
ΔvapH | 26.05 | kJ/mol | 303.90 | NIST |
ρl | 724.00 | kg/m3 | 288.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.69] | kPa | [220.08; 324.64] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45190e+01 | |||
Coefficient B | -2.72698e+03 | |||
Coefficient C | -2.84640e+01 | |||
Temperature range, min. | 220.08 | |||
Temperature range, max. | 324.64 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 220.08 | Calculated Property |
Pvap | 3.01 | kPa | 231.70 | Calculated Property |
Pvap | 6.21 | kPa | 243.32 | Calculated Property |
Pvap | 11.91 | kPa | 254.93 | Calculated Property |
Pvap | 21.44 | kPa | 266.55 | Calculated Property |
Pvap | 36.53 | kPa | 278.17 | Calculated Property |
Pvap | 59.36 | kPa | 289.79 | Calculated Property |
Pvap | 92.56 | kPa | 301.40 | Calculated Property |
Pvap | 139.18 | kPa | 313.02 | Calculated Property |
Pvap | 202.69 | kPa | 324.64 | Calculated Property |
Pvap | [2.39e-06; 3719.20] | kPa | [127.93; 464.50] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.79811e+01 | |||
Coefficient B | -5.03717e+03 | |||
Coefficient C | -6.52061e+00 | |||
Coefficient D | 5.22467e-06 | |||
Temperature range, min. | 127.93 | |||
Temperature range, max. | 464.50 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
Pvap | 2.39e-06 | kPa | 127.93 | Calculated Property |
Pvap | 3.51e-03 | kPa | 165.33 | Calculated Property |
Pvap | 0.28 | kPa | 202.72 | Calculated Property |
Pvap | 4.78 | kPa | 240.12 | Calculated Property |
Pvap | 34.76 | kPa | 277.52 | Calculated Property |
Pvap | 147.72 | kPa | 314.91 | Calculated Property |
Pvap | 442.23 | kPa | 352.31 | Calculated Property |
Pvap | 1044.21 | kPa | 389.71 | Calculated Property |
Pvap | 2089.87 | kPa | 427.10 | Calculated Property |
Pvap | 3719.20 | kPa | 464.50 | Calculated Property |
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