Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -3258.25 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -3585.99 | kJ/mol | Joback Calculated Property |
ΔfusH° | 14.81 | kJ/mol | Joback Calculated Property |
ΔvapH° | 45.60 ± 0.40 | kJ/mol | NIST |
log10WS | -6.96 | Crippen Calculated Property | |
logPoct/wat | 6.348 | Crippen Calculated Property | |
McVol | 171.170 | ml/mol | McGowan Calculated Property |
Pc | 1562.28 | kPa | Joback Calculated Property |
Tboil | 410.35 | K | Joback Calculated Property |
Tc | 536.18 | K | Joback Calculated Property |
Tfus | 269.11 | K | Joback Calculated Property |
Vc | 0.763 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [430.77; 496.22] | J/mol×K | [410.35; 536.18] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 430 440 450 460 470 480 490 500 450 500 | ||||
Cp,gas | 430.77 | J/mol×K | 410.35 | Joback Calculated Property |
Cp,gas | 443.99 | J/mol×K | 431.32 | Joback Calculated Property |
Cp,gas | 456.22 | J/mol×K | 452.29 | Joback Calculated Property |
Cp,gas | 467.52 | J/mol×K | 473.26 | Joback Calculated Property |
Cp,gas | 477.92 | J/mol×K | 494.24 | Joback Calculated Property |
Cp,gas | 487.48 | J/mol×K | 515.21 | Joback Calculated Property |
Cp,gas | 496.22 | J/mol×K | 536.18 | Joback Calculated Property |
ΔfusH | [1.60; 12.13] | kJ/mol | [146.40; 278.90] | ![]() |
ΔfusH | 1.60 | kJ/mol | 146.40 | NIST |
ΔfusH | 12.13 | kJ/mol | 278.90 | NIST |
ΔfusH | 12.13 | kJ/mol | 278.90 | NIST |
ν | [0.0000008; 0.0000011] | m2/s | [298.15; 318.15] | ![]() |
T(K) Kinematic viscosity (m2/s) 7.50e-7 8.00e-7 8.50e-7 9.00e-7 9.50e-7 1.00e-6 1.05e-6 300 305 310 315 | ||||
ν | 0.0000011 | m2/s | 298.15 | Viscosi... |
ν | 0.0000010 | m2/s | 303.15 | Viscosi... |
ν | 0.0000009 | m2/s | 308.15 | Viscosi... |
ν | 0.0000008 | m2/s | 313.15 | Viscosi... |
ν | 0.0000008 | m2/s | 318.15 | Viscosi... |
Pvap | [0.38; 4.70] | kPa | [288.22; 332.78] | ![]() |
T(K) Vapor pressure (kPa) 0 1 2 3 4 5 300 320 | ||||
Pvap | 0.38 | kPa | 288.22 | Densiti... |
Pvap | 0.54 | kPa | 293.20 | Densiti... |
Pvap | 0.69 | kPa | 298.08 | Densiti... |
Pvap | 0.98 | kPa | 303.26 | Densiti... |
Pvap | 1.30 | kPa | 308.22 | Densiti... |
Pvap | 1.67 | kPa | 313.18 | Densiti... |
Pvap | 2.24 | kPa | 318.09 | Densiti... |
Pvap | 2.89 | kPa | 322.92 | Densiti... |
Pvap | 3.69 | kPa | 327.88 | Densiti... |
Pvap | 4.70 | kPa | 332.78 | Densiti... |
ρl | [1869.53; 1926.65] | kg/m3 | [288.63; 311.72] | ![]() |
T(K) Liquid Density (kg/m3) 1870 1880 1890 1900 1910 1920 1930 290 300 310 | ||||
ρl | 1926.65 | kg/m3 | 288.63 | Low pre... |
ρl | 1917.00 | kg/m3 | 292.57 | Low pre... |
ρl | 1906.56 | kg/m3 | 298.78 | Low pre... |
ρl | 1892.19 | kg/m3 | 302.71 | Low pre... |
ρl | 1881.37 | kg/m3 | 307.01 | Low pre... |
ρl | 1869.53 | kg/m3 | 311.72 | Low pre... |
ΔfusS | [10.93; 43.49] | J/mol×K | [146.40; 278.90] | ![]() |
ΔfusS | 10.93 | J/mol×K | 146.40 | NIST |
ΔfusS | 43.49 | J/mol×K | 278.90 | NIST |
γ | [0.02; 0.02] | N/m | [287.15; 318.55] | ![]() |
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.02 290 300 310 | ||||
γ | 0.02 | N/m | 287.15 | Surface... |
γ | 0.02 | N/m | 292.75 | Surface... |
γ | 0.02 | N/m | 298.35 | Surface... |
γ | 0.02 | N/m | 303.35 | Surface... |
γ | 0.02 | N/m | 308.45 | Surface... |
γ | 0.02 | N/m | 313.45 | Surface... |
γ | 0.02 | N/m | 318.55 | Surface... |
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