Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2790 | KDB | |
μ | 0.30 | debye | KDB |
ΔfG° | -1014.34 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -1114.00 ± 10.00 | kJ/mol | NIST |
ΔfusH° | 5.70 | kJ/mol | Joback Calculated Property |
ΔvapH° | 17.75 | kJ/mol | Joback Calculated Property |
IE | [12.60; 12.96] | eV |
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IE | 12.60 | eV | NIST |
IE | 12.96 | eV | NIST |
log10WS | -2.28 | Crippen Calculated Property | |
logPoct/wat | 2.380 | Crippen Calculated Property | |
McVol | 60.130 | ml/mol | McGowan Calculated Property |
Pc | [3120.00; 3229.00] | kPa |
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Pc | 3229.00 | kPa | KDB |
Pc | 3120.00 ± 8.00 | kPa | NIST |
Pc | 3157.29 ± 7.09 | kPa | NIST |
ρc | [603.96; 613.08] | kg/m3 |
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ρc | 603.96 ± 4.63 | kg/m3 | NIST |
ρc | 613.08 ± 1.50 | kg/m3 | NIST |
Inp | 270.00 | NIST | |
S°liquid | 248.03 | J/mol×K | NIST |
Tboil | [235.00; 263.00] | K |
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Tboil | 235.20 | K | KDB |
Tboil | 235.50 ± 0.50 | K | NIST |
Tboil | 235.20 | K | NIST |
Tboil | 235.00 ± 3.00 | K | NIST |
Tboil | 263.00 ± 3.00 | K | NIST |
Tc | [352.94; 353.20] | K |
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Tc | 353.20 | K | KDB |
Tc | 352.94 ± 0.05 | K | NIST |
Tc | 353.10 ± 0.15 | K | NIST |
Tfus | 173.71 | K | KDB |
Ttriple | [173.71; 173.71] | K |
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Ttriple | 173.71 | K | KDB |
Ttriple | 173.71 ± 0.05 | K | NIST |
Vc | 0.252 | m3/kmol | KDB |
Zc | 0.2770840 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [99.25; 130.23] | J/mol×K | [272.48; 416.43] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 100 105 110 115 120 125 130 300 350 400 | ||||
Cp,gas | 99.25 | J/mol×K | 272.48 | Joback Calculated Property |
Cp,gas | 105.39 | J/mol×K | 296.47 | Joback Calculated Property |
Cp,gas | 111.12 | J/mol×K | 320.46 | Joback Calculated Property |
Cp,gas | 116.46 | J/mol×K | 344.46 | Joback Calculated Property |
Cp,gas | 121.41 | J/mol×K | 368.45 | Joback Calculated Property |
Cp,gas | 126.00 | J/mol×K | 392.44 | Joback Calculated Property |
Cp,gas | 130.23 | J/mol×K | 416.43 | Joback Calculated Property |
Cp,liquid | 145.27 | J/mol×K | 234.04 | NIST |
ΔfusH | [1.88; 2.63] | kJ/mol | [80.24; 173.70] | ![]() |
ΔfusH | 2.63 | kJ/mol | 80.24 | NIST |
ΔfusH | 1.88 | kJ/mol | 173.70 | NIST |
ΔfusH | 1.88 | kJ/mol | 173.70 | NIST |
ΔvapH | [19.40; 20.90] | kJ/mol | [205.50; 332.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 19.5 20 20.5 21 250 300 | ||||
ΔvapH | 20.90 | kJ/mol | 205.50 | NIST |
ΔvapH | 20.90 | kJ/mol | 206.00 | NIST |
ΔvapH | 19.40 ± 0.10 | kJ/mol | 234.00 | NIST |
ΔvapH | 19.41 | kJ/mol | 234.04 | NIST |
ΔvapH | 19.46 | kJ/mol | 234.70 | KDB |
ΔvapH | 20.10 | kJ/mol | 249.50 | NIST |
ΔvapH | 19.70 | kJ/mol | 289.50 | NIST |
ΔvapH | 19.70 | kJ/mol | 332.50 | NIST |
Pvap | [148.60; 2077.50] | kPa | [243.15; 333.15] | ![]() |
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 260 280 300 320 | ||||
Pvap | 148.60 | kPa | 243.15 | Measure... |
Pvap | 219.90 | kPa | 253.15 | Measure... |
Pvap | 314.60 | kPa | 263.15 | Measure... |
Pvap | 439.40 | kPa | 273.15 | Measure... |
Pvap | 594.92 | kPa | 283.15 | Measure... |
Pvap | 789.30 | kPa | 293.15 | Measure... |
Pvap | 1028.40 | kPa | 303.15 | Measure... |
Pvap | 1317.90 | kPa | 313.15 | Measure... |
Pvap | 1664.90 | kPa | 323.15 | Measure... |
Pvap | 2077.50 | kPa | 333.15 | Measure... |
ρl | 1260.00 | kg/m3 | 303.00 | KDB |
ΔfusS | [10.79; 32.76] | J/mol×K | [80.24; 173.70] | ![]() |
ΔfusS | 32.76 | J/mol×K | 80.24 | NIST |
ΔfusS | 10.79 | J/mol×K | 173.70 | NIST |
γ | 0.01 | N/m | 298.20 | KDB |
ΔvapS | 82.93 | J/mol×K | 234.04 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 2775.28] | kPa | [168.03; 353.10] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38962e+01 | |||
Coefficient B | -1.96705e+03 | |||
Coefficient C | -2.34850e+01 | |||
Temperature range, min. | 168.03 | |||
Temperature range, max. | 353.10 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 250 300 350 | ||||
Pvap | 1.33 | kPa | 168.03 | Calculated Property |
Pvap | 7.26 | kPa | 188.59 | Calculated Property |
Pvap | 27.17 | kPa | 209.16 | Calculated Property |
Pvap | 78.13 | kPa | 229.72 | Calculated Property |
Pvap | 185.51 | kPa | 250.28 | Calculated Property |
Pvap | 381.50 | kPa | 270.85 | Calculated Property |
Pvap | 702.35 | kPa | 291.41 | Calculated Property |
Pvap | 1185.30 | kPa | 311.97 | Calculated Property |
Pvap | 1865.78 | kPa | 332.54 | Calculated Property |
Pvap | 2775.28 | kPa | 353.10 | Calculated Property |
Pvap | [2.23; 3180.82] | kPa | [174.00; 353.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.94742e+01 | |||
Coefficient B | -4.08741e+03 | |||
Coefficient C | -8.85890e+00 | |||
Coefficient D | 1.71756e-05 | |||
Temperature range, min. | 174.00 | |||
Temperature range, max. | 353.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 250 300 350 | ||||
Pvap | 2.23 | kPa | 174.00 | Calculated Property |
Pvap | 10.77 | kPa | 193.89 | Calculated Property |
Pvap | 37.03 | kPa | 213.78 | Calculated Property |
Pvap | 99.88 | kPa | 233.67 | Calculated Property |
Pvap | 225.62 | kPa | 253.56 | Calculated Property |
Pvap | 446.93 | kPa | 273.44 | Calculated Property |
Pvap | 802.34 | kPa | 293.33 | Calculated Property |
Pvap | 1337.24 | kPa | 313.22 | Calculated Property |
Pvap | 2106.78 | kPa | 333.11 | Calculated Property |
Pvap | 3180.82 | kPa | 353.00 | Calculated Property |
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