Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2690 | KDB | |
AP | 313.050 | K | KDB |
ΔcH°liquid | -4590.10 ± 1.30 | kJ/mol | NIST |
ΔfG° | 45.76 | kJ/mol | KDB |
Δc,grossH | 4590.10 | kJ/mol | KDB |
Δc,netH | 4282.031 | kJ/mol | KDB |
ΔfH°gas | [-129.60; -129.50] | kJ/mol |
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ΔfH°gas | -129.60 | kJ/mol | KDB |
ΔfH°gas | -129.50 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -165.40 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 8.89 | kJ/mol | Joback Calculated Property |
ΔvapH° | [35.80; 35.90] | kJ/mol |
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ΔvapH° | 35.80 | kJ/mol | NIST |
ΔvapH° | 35.90 | kJ/mol | NIST |
IE | 9.92 ± 0.05 | eV | NIST |
log10WS | -2.16 | Crippen Calculated Property | |
logPoct/wat | 2.442 | Crippen Calculated Property | |
McVol | 98.630 | ml/mol | McGowan Calculated Property |
Pc | 3440.00 | kPa | KDB |
Inp | [710.76; 734.00] |
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|
Inp | Outlier 711.00 | NIST | |
Inp | 719.50 | NIST | |
Inp | 723.80 | NIST | |
Inp | 718.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 720.00 | NIST | |
Inp | 724.20 | NIST | |
Inp | 721.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 724.00 | NIST | |
Inp | 719.00 | NIST | |
Inp | 721.40 | NIST | |
Inp | 723.20 | NIST | |
Inp | 725.20 | NIST | |
Inp | 717.00 | NIST | |
Inp | 718.00 | NIST | |
Inp | 720.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 724.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 722.60 | NIST | |
Inp | 723.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 720.00 | NIST | |
Inp | 720.80 | NIST | |
Inp | 724.20 | NIST | |
Inp | 729.10 | NIST | |
Inp | 730.70 | NIST | |
Inp | 723.00 | NIST | |
Inp | 724.80 | NIST | |
Inp | 724.80 | NIST | |
Inp | Outlier 733.00 | NIST | |
Inp | 723.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 719.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 723.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 721.60 | NIST | |
Inp | 719.00 | NIST | |
Inp | Outlier 734.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 715.00 | NIST | |
Inp | Outlier 732.00 | NIST | |
Inp | 716.70 | NIST | |
Inp | 720.20 | NIST | |
Inp | 714.94 | NIST | |
Inp | 722.90 | NIST | |
Inp | 719.40 | NIST | |
Inp | Outlier 710.76 | NIST | |
Inp | 713.09 | NIST | |
Inp | 714.60 | NIST | |
Inp | 715.40 | NIST | |
Inp | 717.85 | NIST | |
Inp | 719.43 | NIST | |
Inp | 715.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 720.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 720.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 721.00 | NIST | |
Inp | 724.00 | NIST | |
Inp | 717.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | Outlier 711.00 | NIST | |
Inp | 722.00 | NIST | |
S°gas | 366.14 | J/mol×K | NIST |
S°liquid | 269.16 | J/mol×K | NIST |
Tboil | [372.25; 372.80] | K |
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Tboil | 372.70 | K | KDB |
Tboil | 372.70 | K | NIST |
Tboil | 372.80 ± 0.50 | K | NIST |
Tboil | 372.50 ± 0.40 | K | NIST |
Tboil | 372.60 ± 0.40 | K | NIST |
Tboil | 372.40 ± 0.40 | K | NIST |
Tboil | 372.75 ± 0.30 | K | NIST |
Tboil | 372.68 ± 0.02 | K | NIST |
Tboil | 372.25 ± 0.40 | K | NIST |
Tboil | 372.75 ± 0.30 | K | NIST |
Tboil | 372.38 ± 0.30 | K | NIST |
Tboil | 372.45 ± 0.20 | K | NIST |
Tboil | 372.38 ± 0.30 | K | NIST |
Tboil | 372.40 ± 0.50 | K | NIST |
Tc | 564.80 | K | KDB |
Tfus | [204.00; 327.00] | K |
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Tfus | 219.30 | K | KDB |
Tfus | 205.00 ± 4.00 | K | NIST |
Tfus | 209.00 ± 4.00 | K | NIST |
Tfus | 204.00 ± 4.00 | K | NIST |
Tfus | 219.13 ± 0.20 | K | NIST |
Tfus | Outlier 327.00 ± 0.06 | K | NIST |
Tfus | 219.13 ± 0.50 | K | NIST |
Tfus | 220.70 ± 2.00 | K | NIST |
Tfus | 220.70 ± 2.00 | K | NIST |
Tfus | 211.00 ± 6.00 | K | NIST |
Ttriple | [219.43; 219.45] | K |
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Ttriple | 219.45 ± 0.05 | K | NIST |
Ttriple | 219.43 ± 0.06 | K | NIST |
Ttriple | 219.43 ± 0.04 | K | NIST |
Ttriple | 219.43 ± 0.04 | K | NIST |
Vc | 0.368 | m3/kmol | KDB |
Zc | 0.2695720 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [173.95; 256.86] | J/mol×K | [370.17; 563.52] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 180 200 220 240 260 400 450 500 550 | ||||
Cp,gas | 173.95 | J/mol×K | 370.17 | Joback Calculated Property |
Cp,gas | 189.42 | J/mol×K | 402.40 | Joback Calculated Property |
Cp,gas | 204.20 | J/mol×K | 434.62 | Joback Calculated Property |
Cp,gas | 218.32 | J/mol×K | 466.85 | Joback Calculated Property |
Cp,gas | 231.80 | J/mol×K | 499.07 | Joback Calculated Property |
Cp,gas | 244.64 | J/mol×K | 531.30 | Joback Calculated Property |
Cp,gas | 256.86 | J/mol×K | 563.52 | Joback Calculated Property |
Cp,liquid | 190.66 | J/mol×K | 302.84 | NIST |
η | [0.0002650; 0.0017720] | Pa×s | [175.31; 370.17] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 200 250 300 350 | ||||
η | 0.0017720 | Pa×s | 175.31 | Joback Calculated Property |
η | 0.0010080 | Pa×s | 207.79 | Joback Calculated Property |
η | 0.0006678 | Pa×s | 240.26 | Joback Calculated Property |
η | 0.0004881 | Pa×s | 272.74 | Joback Calculated Property |
η | 0.0003813 | Pa×s | 305.22 | Joback Calculated Property |
η | 0.0003124 | Pa×s | 337.69 | Joback Calculated Property |
η | 0.0002650 | Pa×s | 370.17 | Joback Calculated Property |
ΔfusH | [1.66; 6.65] | kJ/mol | [141.50; 219.40] | ![]() |
ΔfusH | 6.65 | kJ/mol | 141.50 | NIST |
ΔfusH | 1.66 | kJ/mol | 219.40 | NIST |
ΔfusH | 1.66 | kJ/mol | 219.40 | NIST |
ΔvapH | [31.70; 35.50] | kJ/mol | [334.00; 372.70] | ![]() |
ΔvapH | 35.50 | kJ/mol | 334.00 | NIST |
ΔvapH | 35.20 | kJ/mol | 335.50 | NIST |
ΔvapH | 31.70 | kJ/mol | 372.70 | KDB |
n0 | 1.41963 | 298.15 | KDB | |
ρl | 777.00 | kg/m3 | 289.00 | KDB |
ΔfusS | [7.55; 47.01] | J/mol×K | [141.50; 219.40] | ![]() |
ΔfusS | 47.01 | J/mol×K | 141.50 | NIST |
ΔfusS | 7.55 | J/mol×K | 219.40 | NIST |
γ | 0.02 | N/m | 298.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [270.04; 398.18] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41919e+01 | |||
Coefficient B | -3.14938e+03 | |||
Coefficient C | -4.35340e+01 | |||
Temperature range, min. | 270.04 | |||
Temperature range, max. | 398.18 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 270.04 | Calculated Property |
Pvap | 3.03 | kPa | 284.28 | Calculated Property |
Pvap | 6.30 | kPa | 298.52 | Calculated Property |
Pvap | 12.11 | kPa | 312.75 | Calculated Property |
Pvap | 21.79 | kPa | 326.99 | Calculated Property |
Pvap | 37.07 | kPa | 341.23 | Calculated Property |
Pvap | 60.07 | kPa | 355.47 | Calculated Property |
Pvap | 93.34 | kPa | 369.70 | Calculated Property |
Pvap | 139.79 | kPa | 383.94 | Calculated Property |
Pvap | 202.67 | kPa | 398.18 | Calculated Property |
Pvap | [0.02; 3435.73] | kPa | [219.26; 565.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.19973e+01 | |||
Coefficient B | -6.92394e+03 | |||
Coefficient C | -1.01145e+01 | |||
Coefficient D | 7.80447e-06 | |||
Temperature range, min. | 219.26 | |||
Temperature range, max. | 565.15 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 | ||||
Pvap | 0.02 | kPa | 219.26 | Calculated Property |
Pvap | 0.60 | kPa | 257.69 | Calculated Property |
Pvap | 5.70 | kPa | 296.12 | Calculated Property |
Pvap | 29.41 | kPa | 334.56 | Calculated Property |
Pvap | 102.12 | kPa | 372.99 | Calculated Property |
Pvap | 271.40 | kPa | 411.42 | Calculated Property |
Pvap | 599.71 | kPa | 449.85 | Calculated Property |
Pvap | 1164.56 | kPa | 488.29 | Calculated Property |
Pvap | 2064.98 | kPa | 526.72 | Calculated Property |
Pvap | 3435.73 | kPa | 565.15 | Calculated Property |
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