Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | [-4151.00; -4132.60] | kJ/mol | |
ΔcH°liquid | -4133.80 | kJ/mol | NIST |
ΔcH°liquid | -4132.60 ± 1.50 | kJ/mol | NIST |
ΔcH°liquid | -4151.00 | kJ/mol | NIST |
ΔfG° | 20.61 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-110.80; -109.70] | kJ/mol | |
ΔfH°gas | -109.70 | kJ/mol | NIST |
ΔfH°gas | -110.80 ± 1.80 | kJ/mol | NIST |
ΔfH°liquid | [-152.00; -150.90] | kJ/mol | |
ΔfH°liquid | -150.90 ± 0.84 | kJ/mol | NIST |
ΔfH°liquid | -152.00 ± 1.70 | kJ/mol | NIST |
ΔfusH° | 12.75 | kJ/mol | Joback Calculated Property |
ΔvapH° | [41.10; 41.26] | kJ/mol | |
ΔvapH° | 41.26 | kJ/mol | NIST |
ΔvapH° | 41.10 | kJ/mol | NIST |
ΔvapH° | 41.10 | kJ/mol | NIST |
ΔvapH° | 41.20 | kJ/mol | NIST |
log10WS | -1.99 | Crippen Calculated Property | |
logPoct/wat | 2.106 | Crippen Calculated Property | |
McVol | 97.660 | ml/mol | McGowan Calculated Property |
Pc | 3745.38 | kPa | Joback Calculated Property |
Inp | [795.00; 828.80] | ||
Inp | 821.70 | NIST | |
Inp | 828.80 | NIST | |
Inp | 814.00 | NIST | |
Inp | 817.00 | NIST | |
Inp | 818.90 | NIST | |
Inp | 821.10 | NIST | |
Inp | 824.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 827.00 | NIST | |
Inp | 828.00 | NIST | |
Inp | 816.00 | NIST | |
Inp | 826.00 | NIST | |
Inp | 822.00 | NIST | |
Inp | 814.00 | NIST | |
Inp | 817.00 | NIST | |
Inp | 803.00 | NIST | |
Inp | 822.00 | NIST | |
Inp | 819.00 | NIST | |
Inp | 822.00 | NIST | |
Inp | Outlier 795.00 | NIST | |
I | [1039.00; 1063.00] | ||
I | 1052.90 | NIST | |
I | 1047.90 | NIST | |
I | 1039.00 | NIST | |
I | 1063.00 | NIST | |
S°liquid | 310.37 | J/mol×K | NIST |
Tboil | [397.00; 399.80] | K | |
Tboil | 399.20 | K | NIST |
Tboil | 399.00 | K | NIST |
Tboil | 399.80 | K | NIST |
Tboil | 397.00 ± 2.50 | K | NIST |
Tboil | 398.00 ± 1.00 | K | NIST |
Tc | 597.70 | K | NIST |
Tfus | [197.50; 197.50] | K | |
Tfus | 197.50 ± 0.50 | K | NIST |
Tfus | 197.50 ± 0.30 | K | NIST |
Ttriple | [197.45; 197.46] | K | |
Ttriple | 197.45 ± 0.02 | K | NIST |
Ttriple | 197.46 ± 0.02 | K | NIST |
Vc | 0.369 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [168.36; 222.90] | J/mol×K | [376.66; 566.46] | |
Cp,gas | 168.36 | J/mol×K | 376.66 | Joback Calculated Property |
Cp,gas | 178.44 | J/mol×K | 408.29 | Joback Calculated Property |
Cp,gas | 188.11 | J/mol×K | 439.93 | Joback Calculated Property |
Cp,gas | 197.38 | J/mol×K | 471.56 | Joback Calculated Property |
Cp,gas | 206.26 | J/mol×K | 503.19 | Joback Calculated Property |
Cp,gas | 214.76 | J/mol×K | 534.82 | Joback Calculated Property |
Cp,gas | 222.90 | J/mol×K | 566.46 | Joback Calculated Property |
Cp,liquid | 201.17 | J/mol×K | 296.21 | NIST |
ΔfusH | [17.53; 17.53] | kJ/mol | [197.46; 197.50] | |
ΔfusH | 17.53 | kJ/mol | 197.46 | NIST |
ΔfusH | 17.53 | kJ/mol | 197.50 | NIST |
ΔfusH | 17.53 | kJ/mol | 197.50 | NIST |
ΔvapH | [34.88; 40.60] | kJ/mol | [356.00; 400.00] | |
ΔvapH | 37.10 ± 0.10 | kJ/mol | 356.00 | NIST |
ΔvapH | 40.60 | kJ/mol | 363.00 | NIST |
ΔvapH | 36.40 ± 0.10 | kJ/mol | 376.00 | NIST |
ΔvapH | 38.10 | kJ/mol | 393.50 | NIST |
ΔvapH | 34.88 | kJ/mol | 399.80 | NIST |
ΔvapH | 34.90 ± 0.10 | kJ/mol | 400.00 | NIST |
ΔfusS | 88.78 | J/mol×K | 197.46 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [300.23; 422.88] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.54679e+01 | |||
Coefficient B | -3.76382e+03 | |||
Coefficient C | -5.22920e+01 | |||
Temperature range, min. | 300.23 | |||
Temperature range, max. | 422.88 | |||
Pvap | 1.33 | kPa | 300.23 | Calculated Property |
Pvap | 2.94 | kPa | 313.86 | Calculated Property |
Pvap | 6.00 | kPa | 327.49 | Calculated Property |
Pvap | 11.43 | kPa | 341.11 | Calculated Property |
Pvap | 20.56 | kPa | 354.74 | Calculated Property |
Pvap | 35.16 | kPa | 368.37 | Calculated Property |
Pvap | 57.52 | kPa | 382.00 | Calculated Property |
Pvap | 90.50 | kPa | 395.62 | Calculated Property |
Pvap | 137.53 | kPa | 409.25 | Calculated Property |
Pvap | 202.67 | kPa | 422.88 | Calculated Property |
Pvap | [1.96e-04; 3365.99] | kPa | [197.45; 598.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.71980e+01 | |||
Coefficient B | -7.40124e+03 | |||
Coefficient C | -9.16808e+00 | |||
Coefficient D | 5.36099e-06 | |||
Temperature range, min. | 197.45 | |||
Temperature range, max. | 598.00 | |||
Pvap | 1.96e-04 | kPa | 197.45 | Calculated Property |
Pvap | 0.03 | kPa | 241.96 | Calculated Property |
Pvap | 0.93 | kPa | 286.46 | Calculated Property |
Pvap | 9.29 | kPa | 330.97 | Calculated Property |
Pvap | 49.00 | kPa | 375.47 | Calculated Property |
Pvap | 171.33 | kPa | 419.98 | Calculated Property |
Pvap | 454.74 | kPa | 464.48 | Calculated Property |
Pvap | 998.64 | kPa | 508.99 | Calculated Property |
Pvap | 1921.00 | kPa | 553.49 | Calculated Property |
Pvap | 3365.99 | kPa | 598.00 | Calculated Property |
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