Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4510 | KDB | |
AP | 351.350 | K | KDB |
ΔfG° | 30.88 | kJ/mol | Joback Calculated Property |
Δc,grossH | 6775.15 | kJ/mol | KDB |
Δc,netH | 6291.021 | kJ/mol | KDB |
ΔfH°gas | -255.01 | kJ/mol | Joback Calculated Property |
ΔfusH° | 18.13 | kJ/mol | Joback Calculated Property |
ΔvapH° | [49.72; 50.20] | kJ/mol | |
ΔvapH° | 49.72 | kJ/mol | NIST |
ΔvapH° | 50.20 | kJ/mol | NIST |
log10WS | -3.77 | Crippen Calculated Property | |
logPoct/wat | 4.003 | Crippen Calculated Property | |
McVol | 151.760 | ml/mol | McGowan Calculated Property |
Pc | 2140.00 | kPa | KDB |
Inp | [958.00; 980.00] | ||
Inp | 970.40 | NIST | |
Inp | 970.50 | NIST | |
Inp | 970.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | 967.00 | NIST | |
Inp | Outlier 979.00 | NIST | |
Inp | 974.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | Outlier 980.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 971.20 | NIST | |
Inp | 971.30 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.40 | NIST | |
Inp | 970.40 | NIST | |
Inp | 970.60 | NIST | |
Inp | 972.50 | NIST | |
Inp | 970.40 | NIST | |
Inp | 971.30 | NIST | |
Inp | 969.60 | NIST | |
Inp | 970.20 | NIST | |
Inp | 973.00 | NIST | |
Inp | Outlier 958.00 | NIST | |
Inp | 970.42 | NIST | |
Inp | 970.42 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 977.00 | NIST | |
Inp | 971.92 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 977.20 | NIST | |
Inp | Outlier 979.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | Outlier 962.00 | NIST | |
Inp | 972.80 | NIST | |
Inp | 969.00 | NIST | |
Inp | 971.20 | NIST | |
Inp | 970.50 | NIST | |
Inp | 971.70 | NIST | |
Inp | 974.20 | NIST | |
Inp | 972.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 971.80 | NIST | |
Inp | 972.15 | NIST | |
Inp | 972.23 | NIST | |
Inp | 971.40 | NIST | |
Inp | 971.74 | NIST | |
Inp | 971.85 | NIST | |
Inp | 970.00 | NIST | |
Inp | 968.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | Outlier 960.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 975.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 974.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 972.10 | NIST | |
Inp | 967.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | Outlier 964.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 968.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 971.40 | NIST | |
Inp | 977.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 972.00 | NIST | |
Inp | 966.00 | NIST | |
Inp | 971.00 | NIST | |
Inp | 969.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 976.00 | NIST | |
Inp | 970.00 | NIST | |
I | [965.00; 983.00] | ||
I | 983.00 | NIST | |
I | 969.00 | NIST | |
I | 965.00 | NIST | |
I | 983.00 | NIST | |
I | 969.00 | NIST | |
S°liquid | 427.20 | J/mol×K | NIST |
Tboil | 441.00 | K | KDB |
Tc | [613.40; 613.60] | K | |
Tc | 613.40 | K | KDB |
Tc | 613.60 | K | NIST |
Tfus | [183.15; 188.49] | K | |
Tfus | 188.00 | K | KDB |
Tfus | 188.49 ± 0.20 | K | NIST |
Tfus | 183.15 ± 0.50 | K | NIST |
Tfus | 188.29 ± 0.20 | K | NIST |
Ttriple | 188.50 ± 0.20 | K | NIST |
Vc | 0.582 | m3/kmol | KDB |
Zc | 0.2442060 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [315.29; 399.91] | J/mol×K | [427.76; 593.73] | |
T(K) Ideal gas heat capacity (J/mol×K) 320 340 360 380 400 450 500 550 | ||||
Cp,gas | 315.29 | J/mol×K | 427.76 | Joback Calculated Property |
Cp,gas | 330.79 | J/mol×K | 455.42 | Joback Calculated Property |
Cp,gas | 345.71 | J/mol×K | 483.08 | Joback Calculated Property |
Cp,gas | 360.07 | J/mol×K | 510.75 | Joback Calculated Property |
Cp,gas | 373.88 | J/mol×K | 538.41 | Joback Calculated Property |
Cp,gas | 387.16 | J/mol×K | 566.07 | Joback Calculated Property |
Cp,gas | 399.91 | J/mol×K | 593.73 | Joback Calculated Property |
Cp,liquid | 308.99 | J/mol×K | 298.10 | NIST |
η | [0.0002265; 0.0108083] | Pa×s | [187.46; 427.76] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 300 400 | ||||
η | 0.0108083 | Pa×s | 187.46 | Joback Calculated Property |
η | 0.0032190 | Pa×s | 227.51 | Joback Calculated Property |
η | 0.0013777 | Pa×s | 267.56 | Joback Calculated Property |
η | 0.0007355 | Pa×s | 307.61 | Joback Calculated Property |
η | 0.0004537 | Pa×s | 347.66 | Joback Calculated Property |
η | 0.0003093 | Pa×s | 387.71 | Joback Calculated Property |
η | 0.0002265 | Pa×s | 427.76 | Joback Calculated Property |
ΔfusH | [18.70; 18.70] | kJ/mol | [188.50; 188.50] | |
ΔfusH | 18.70 | kJ/mol | 188.50 | NIST |
ΔfusH | 18.70 | kJ/mol | 188.50 | NIST |
ΔvapH | [38.26; 47.30] | kJ/mol | [328.00; 441.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 38 40 42 44 46 48 350 400 | ||||
ΔvapH | 47.30 ± 0.20 | kJ/mol | 328.00 | NIST |
ΔvapH | 46.20 ± 0.20 | kJ/mol | 343.00 | NIST |
ΔvapH | 45.10 ± 0.20 | kJ/mol | 358.00 | NIST |
ΔvapH | 39.12 | kJ/mol | 441.00 | KDB |
ΔvapH | 38.26 | kJ/mol | 441.00 | NIST |
n0 | 1.41030 | 298.15 | KDB | |
ΔfusS | 99.20 | J/mol×K | 188.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [323.99; 469.90] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45072e+01 | |||
Coefficient B | -3.79773e+03 | |||
Coefficient C | -5.69090e+01 | |||
Temperature range, min. | 323.99 | |||
Temperature range, max. | 469.90 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 323.99 | Calculated Property |
Pvap | 3.01 | kPa | 340.20 | Calculated Property |
Pvap | 6.22 | kPa | 356.41 | Calculated Property |
Pvap | 11.92 | kPa | 372.63 | Calculated Property |
Pvap | 21.45 | kPa | 388.84 | Calculated Property |
Pvap | 36.55 | kPa | 405.05 | Calculated Property |
Pvap | 59.38 | kPa | 421.26 | Calculated Property |
Pvap | 92.58 | kPa | 437.48 | Calculated Property |
Pvap | 139.18 | kPa | 453.69 | Calculated Property |
Pvap | 202.66 | kPa | 469.90 | Calculated Property |
Pvap | [5.74e-07; 2188.73] | kPa | [188.35; 613.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.11505e+02 | |||
Coefficient B | -9.76977e+03 | |||
Coefficient C | -1.41847e+01 | |||
Coefficient D | 8.42650e-06 | |||
Temperature range, min. | 188.35 | |||
Temperature range, max. | 613.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 200 400 600 | ||||
Pvap | 5.74e-07 | kPa | 188.35 | Calculated Property |
Pvap | 9.29e-04 | kPa | 235.53 | Calculated Property |
Pvap | 0.09 | kPa | 282.72 | Calculated Property |
Pvap | 1.74 | kPa | 329.90 | Calculated Property |
Pvap | 14.07 | kPa | 377.08 | Calculated Property |
Pvap | 64.82 | kPa | 424.27 | Calculated Property |
Pvap | 207.81 | kPa | 471.45 | Calculated Property |
Pvap | 524.56 | kPa | 518.63 | Calculated Property |
Pvap | 1129.44 | kPa | 565.82 | Calculated Property |
Pvap | 2188.73 | kPa | 613.00 | Calculated Property |
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