Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-3860.20; -3857.00] | kJ/mol | |
ΔcH°liquid | -3860.20 ± 1.10 | kJ/mol | NIST |
ΔcH°liquid | -3857.00 ± 0.80 | kJ/mol | NIST |
ΔfG° | -17.52 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-182.40; -179.20] | kJ/mol | |
ΔfH°gas | -179.20 ± 1.20 | kJ/mol | NIST |
ΔfH°gas | -182.40 | kJ/mol | NIST |
ΔfH°liquid | [-219.00; -215.80] | kJ/mol | |
ΔfH°liquid | -215.80 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -219.00 ± 0.80 | kJ/mol | NIST |
ΔfusH° | 11.20 | kJ/mol | Joback Calculated Property |
ΔvapH° | 30.69 | kJ/mol | Joback Calculated Property |
log10WS | -1.77 | Crippen Calculated Property | |
logPoct/wat | 1.947 | Crippen Calculated Property | |
McVol | 96.970 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 3200.00 ± 250.00 | kPa | NIST |
ρc | 261.11 ± 12.02 | kg/m3 | NIST |
Inp | [671.00; 695.00] | ||
Inp | 695.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 695.00 | NIST | |
I | 858.00 | NIST | |
Tboil | [366.00; 367.10] | K | |
Tboil | 367.00 | K | NIST |
Tboil | 366.00 | K | NIST |
Tboil | 367.10 | K | NIST |
Tc | 540.50 ± 2.00 | K | NIST |
Tfus | 177.85 | K | Joback Calculated Property |
Vc | 0.370 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [168.37; 221.32] | J/mol×K | [355.78; 523.68] | |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 220 400 450 500 | ||||
Cp,gas | 168.37 | J/mol×K | 355.78 | Joback Calculated Property |
Cp,gas | 177.92 | J/mol×K | 383.76 | Joback Calculated Property |
Cp,gas | 187.18 | J/mol×K | 411.75 | Joback Calculated Property |
Cp,gas | 196.15 | J/mol×K | 439.73 | Joback Calculated Property |
Cp,gas | 204.82 | J/mol×K | 467.71 | Joback Calculated Property |
Cp,gas | 213.21 | J/mol×K | 495.69 | Joback Calculated Property |
Cp,gas | 221.32 | J/mol×K | 523.68 | Joback Calculated Property |
Cp,liquid | 231.80 | J/mol×K | 298.15 | NIST |
η | [0.0002123; 0.0029205] | Pa×s | [177.85; 355.78] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 200 250 300 350 | ||||
η | 0.0029205 | Pa×s | 177.85 | Joback Calculated Property |
η | 0.0013807 | Pa×s | 207.51 | Joback Calculated Property |
η | 0.0007872 | Pa×s | 237.16 | Joback Calculated Property |
η | 0.0005086 | Pa×s | 266.81 | Joback Calculated Property |
η | 0.0003585 | Pa×s | 296.47 | Joback Calculated Property |
η | 0.0002694 | Pa×s | 326.12 | Joback Calculated Property |
η | 0.0002123 | Pa×s | 355.78 | Joback Calculated Property |
ΔvapH | [29.60; 36.10] | kJ/mol | [318.50; 367.10] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 29 30 31 32 33 34 35 36 320 340 360 | ||||
ΔvapH | 36.10 | kJ/mol | 318.50 | NIST |
ΔvapH | 35.20 ± 0.20 | kJ/mol | 357.00 | NIST |
ΔvapH | 32.50 ± 0.20 | kJ/mol | 357.00 | NIST |
ΔvapH | 29.60 ± 0.20 | kJ/mol | 357.00 | NIST |
ΔvapH | 31.58 | kJ/mol | 367.10 | NIST |
ρl | [758.80; 780.20] | kg/m3 | [298.15; 313.15] | |
T(K) Liquid Density (kg/m3) 760 765 770 775 780 300 305 310 | ||||
ρl | 780.20 | kg/m3 | 298.15 | Densiti... |
ρl | 769.00 | kg/m3 | 303.15 | Density... |
ρl | 774.10 | kg/m3 | 303.15 | Densiti... |
ρl | 763.90 | kg/m3 | 308.15 | Density... |
ρl | 768.20 | kg/m3 | 308.15 | Densiti... |
ρl | 758.80 | kg/m3 | 313.15 | Density... |
ρl | 763.30 | kg/m3 | 313.15 | Densiti... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.62] | kPa | [274.58; 389.11] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54615e+01 | |||
Coefficient B | -3.51136e+03 | |||
Coefficient C | -4.31680e+01 | |||
Temperature range, min. | 274.58 | |||
Temperature range, max. | 389.11 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 274.58 | Calculated Property |
Pvap | 2.94 | kPa | 287.31 | Calculated Property |
Pvap | 6.00 | kPa | 300.03 | Calculated Property |
Pvap | 11.43 | kPa | 312.76 | Calculated Property |
Pvap | 20.57 | kPa | 325.48 | Calculated Property |
Pvap | 35.17 | kPa | 338.21 | Calculated Property |
Pvap | 57.53 | kPa | 350.93 | Calculated Property |
Pvap | 90.49 | kPa | 363.66 | Calculated Property |
Pvap | 137.51 | kPa | 376.38 | Calculated Property |
Pvap | 202.62 | kPa | 389.11 | Calculated Property |
Pvap | [1.31e-04; 3086.33] | kPa | [181.15; 536.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.18610e+01 | |||
Coefficient B | -7.10617e+03 | |||
Coefficient C | -9.96430e+00 | |||
Coefficient D | 7.13053e-06 | |||
Temperature range, min. | 181.15 | |||
Temperature range, max. | 536.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
Pvap | 1.31e-04 | kPa | 181.15 | Calculated Property |
Pvap | 0.02 | kPa | 220.58 | Calculated Property |
Pvap | 0.67 | kPa | 260.01 | Calculated Property |
Pvap | 7.05 | kPa | 299.43 | Calculated Property |
Pvap | 38.90 | kPa | 338.86 | Calculated Property |
Pvap | 141.40 | kPa | 378.29 | Calculated Property |
Pvap | 387.84 | kPa | 417.72 | Calculated Property |
Pvap | 875.73 | kPa | 457.14 | Calculated Property |
Pvap | 1725.20 | kPa | 496.57 | Calculated Property |
Pvap | 3086.33 | kPa | 536.00 | Calculated Property |
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