Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3330 | KDB | |
ΔcH°liquid | -3378.97 | kJ/mol | NIST |
μ | 1.20 | debye | KDB |
ΔfG° | -125.50 | kJ/mol | KDB |
ΔfH°gas | -272.20 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -303.60 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 9.89 | kJ/mol | Joback Calculated Property |
ΔvapH° | [31.39; 31.57] | kJ/mol | |
ΔvapH° | Outlier 31.57 | kJ/mol | NIST |
ΔvapH° | 31.39 | kJ/mol | NIST |
ΔvapH° | 31.40 | kJ/mol | NIST |
ΔvapH° | 31.40 | kJ/mol | NIST |
ΔvapH° | 31.43 ± 0.11 | kJ/mol | NIST |
ΔvapH° | 31.40 ± 0.10 | kJ/mol | NIST |
IE | 9.50 ± 0.10 | eV | NIST |
log10WS | [-0.66; -0.66] | ||
log10WS | -0.66 | Aq. Sol... | |
log10WS | -0.66 | Estimat... | |
logPoct/wat | 1.433 | Crippen Calculated Property | |
McVol | 87.180 | ml/mol | McGowan Calculated Property |
Pc | [3250.00; 3370.00] | kPa | |
Pc | 3370.00 | kPa | KDB |
Pc | 3370.00 ± 6.00 | kPa | NIST |
Pc | 3250.00 ± 40.53 | kPa | NIST |
ρc | 260.13 ± 1.76 | kg/m3 | NIST |
Inp | [566.50; 590.00] | ||
Inp | 590.00 | NIST | |
Inp | 566.50 | NIST | |
Inp | 572.10 | NIST | |
Inp | 590.00 | NIST | |
S°gas | 388.10 | J/mol×K | NIST |
S°liquid | 295.00 | J/mol×K | NIST |
Tboil | [336.30; 336.80] | K | |
Tboil | 336.36 | K | KDB |
Tboil | 336.80 | K | NIST |
Tboil | 336.30 | K | NIST |
Tboil | 336.40 ± 0.50 | K | NIST |
Tc | [500.20; 500.60] | K | |
Tc | 500.23 | K | KDB |
Tc | 500.20 | K | NIST |
Tc | 500.23 ± 0.20 | K | NIST |
Tc | 500.60 ± 0.50 | K | NIST |
Tfus | [145.60; 146.45] | K | |
Tfus | 145.60 | K | KDB |
Tfus | 145.90 | K | Aq. Sol... |
Tfus | 146.45 ± 0.40 | K | NIST |
Ttriple | 145.65 ± 0.05 | K | NIST |
Vc | 0.339 | m3/kmol | KDB |
Zc | 0.2746780 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [147.83; 196.68] | J/mol×K | [336.22; 500.48] | |
T(K) Ideal gas heat capacity (J/mol×K) 150 160 170 180 190 200 350 400 450 500 | ||||
Cp,gas | 147.83 | J/mol×K | 336.22 | Joback Calculated Property |
Cp,gas | 156.52 | J/mol×K | 363.60 | Joback Calculated Property |
Cp,gas | 164.99 | J/mol×K | 390.97 | Joback Calculated Property |
Cp,gas | 173.24 | J/mol×K | 418.35 | Joback Calculated Property |
Cp,gas | 181.27 | J/mol×K | 445.73 | Joback Calculated Property |
Cp,gas | 189.09 | J/mol×K | 473.10 | Joback Calculated Property |
Cp,gas | 196.68 | J/mol×K | 500.48 | Joback Calculated Property |
Cp,liquid | [197.20; 197.50] | J/mol×K | [298.15; 298.15] | |
Cp,liquid | 197.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 197.50 | J/mol×K | 298.15 | NIST |
η | [0.0002124; 0.0030953] | Pa×s | [168.34; 336.22] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 | ||||
η | 0.0030953 | Pa×s | 168.34 | Joback Calculated Property |
η | 0.0014407 | Pa×s | 196.32 | Joback Calculated Property |
η | 0.0008115 | Pa×s | 224.30 | Joback Calculated Property |
η | 0.0005192 | Pa×s | 252.28 | Joback Calculated Property |
η | 0.0003631 | Pa×s | 280.26 | Joback Calculated Property |
η | 0.0002710 | Pa×s | 308.24 | Joback Calculated Property |
η | 0.0002124 | Pa×s | 336.22 | Joback Calculated Property |
ΔfusH | [8.39; 8.39] | kJ/mol | [145.65; 145.70] | |
ΔfusH | 8.39 | kJ/mol | 145.65 | NIST |
ΔfusH | 8.39 | kJ/mol | 145.70 | NIST |
ΔfusH | 8.39 | kJ/mol | 145.70 | NIST |
ΔvapH | [28.94; 33.00] | kJ/mol | [311.50; 336.30] | |
ΔvapH | 33.00 | kJ/mol | 311.50 | NIST |
ΔvapH | 29.00 | kJ/mol | 311.50 | NIST |
ΔvapH | 31.60 | kJ/mol | 314.00 | NIST |
ΔvapH | 28.94 | kJ/mol | 336.30 | NIST |
ρl | 733.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 57.64 | J/mol×K | 145.65 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [250.01; 357.64] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.53548e+01 | |||
Coefficient B | -3.24200e+03 | |||
Coefficient C | -3.48390e+01 | |||
Temperature range, min. | 250.01 | |||
Temperature range, max. | 357.64 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 350 | ||||
Pvap | 1.33 | kPa | 250.01 | Calculated Property |
Pvap | 2.95 | kPa | 261.97 | Calculated Property |
Pvap | 6.02 | kPa | 273.93 | Calculated Property |
Pvap | 11.48 | kPa | 285.89 | Calculated Property |
Pvap | 20.66 | kPa | 297.85 | Calculated Property |
Pvap | 35.31 | kPa | 309.80 | Calculated Property |
Pvap | 57.72 | kPa | 321.76 | Calculated Property |
Pvap | 90.72 | kPa | 333.72 | Calculated Property |
Pvap | 137.70 | kPa | 345.68 | Calculated Property |
Pvap | 202.65 | kPa | 357.64 | Calculated Property |
Pvap | [7.50e-07; 3410.31] | kPa | [145.65; 500.23] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.32471e+02 | |||
Coefficient B | -8.24837e+03 | |||
Coefficient C | -1.81397e+01 | |||
Coefficient D | 1.95507e-05 | |||
Temperature range, min. | 145.65 | |||
Temperature range, max. | 500.23 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 500 | ||||
Pvap | 7.50e-07 | kPa | 145.65 | Calculated Property |
Pvap | 2.17e-03 | kPa | 185.05 | Calculated Property |
Pvap | 0.22 | kPa | 224.45 | Calculated Property |
Pvap | 4.20 | kPa | 263.84 | Calculated Property |
Pvap | 30.21 | kPa | 303.24 | Calculated Property |
Pvap | 123.68 | kPa | 342.64 | Calculated Property |
Pvap | 359.27 | kPa | 382.04 | Calculated Property |
Pvap | 846.38 | kPa | 421.43 | Calculated Property |
Pvap | 1759.30 | kPa | 460.83 | Calculated Property |
Pvap | 3410.31 | kPa | 500.23 | Calculated Property |
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