Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1940 | KDB | |
PAff | [802.10; 805.00] | kJ/mol | |
PAff | 802.10 | kJ/mol | NIST |
PAff | 802.30 ± 4.80 | kJ/mol | NIST |
PAff | 802.30 ± 4.80 | kJ/mol | NIST |
PAff | 805.00 ± 6.70 | kJ/mol | NIST |
Tig | 738.15 | K | KDB |
AP | 288.050 | K | KDB |
BasG | [775.60; 776.30] | kJ/mol | |
BasG | 775.60 | kJ/mol | NIST |
BasG | 776.30 ± 2.70 | kJ/mol | NIST |
BasG | 776.30 ± 2.70 | kJ/mol | NIST |
ΔcH°gas | [-2722.00; -2699.50] | kJ/mol | |
ΔcH°gas | -2699.50 ± 1.00 | kJ/mol | NIST |
ΔcH°gas | -2722.00 | kJ/mol | NIST |
μ | 0.50 | debye | KDB |
LFL | 1.80 | % in Air | KDB |
UFL | 9.60 | % in Air | KDB |
Tflash,oc | 197.04 | K | KDB |
ΔfG° | 58.11 | kJ/mol | KDB |
Δc,grossH | 2679.27 | kJ/mol | KDB |
Δc,netH | 2503.204 | kJ/mol | KDB |
ΔfH°gas | [-17.90; -16.91] | kJ/mol | |
ΔfH°gas | -16.91 | kJ/mol | KDB |
ΔfH°gas | -17.90 ± 1.10 | kJ/mol | NIST |
ΔfusH° | 3.53 | kJ/mol | Joback Calculated Property |
ΔvapH° | 20.60 | kJ/mol | NIST |
IE | [9.17; 9.45] | eV | |
IE | 9.22 ± 0.02 | eV | NIST |
IE | 9.19 | eV | NIST |
IE | 9.24 ± 0.05 | eV | NIST |
IE | 9.24 ± 0.02 | eV | NIST |
IE | 9.24 ± 0.00 | eV | NIST |
IE | 9.19 | eV | NIST |
IE | 9.21 | eV | NIST |
IE | 9.17 | eV | NIST |
IE | 9.23 ± 0.02 | eV | NIST |
IE | 9.23 | eV | NIST |
IE | 9.41 | eV | NIST |
IE | 9.39 | eV | NIST |
IE | Outlier 9.45 | eV | NIST |
log10WS | [-2.33; -2.33] | ||
log10WS | -2.33 | Aq. Sol... | |
log10WS | -2.33 | Estimat... | |
logPoct/wat | 1.582 | Crippen Calculated Property | |
McVol | 62.920 | ml/mol | McGowan Calculated Property |
Pc | [4000.00; 4009.80] | kPa | |
Pc | 4000.00 | kPa | KDB |
Pc | 4009.80 | kPa | Thermod... |
Pc | 4000.00 ± 10.00 | kPa | NIST |
Pc | 4000.31 ± 10.13 | kPa | NIST |
ρc | [233.96; 235.09] | kg/m3 | |
ρc | 235.09 ± 0.56 | kg/m3 | NIST |
ρc | 233.96 ± 2.81 | kg/m3 | NIST |
Inp | [370.00; 400.00] | ||
Inp | 394.00 | NIST | |
Inp | 391.00 | NIST | |
Inp | 389.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 380.00 | NIST | |
Inp | 383.00 | NIST | |
Inp | 383.00 | NIST | |
Inp | 383.00 | NIST | |
Inp | 384.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 382.00 | NIST | |
Inp | 392.00 | NIST | |
Inp | 391.00 | NIST | |
Inp | 384.00 | NIST | |
Inp | 383.00 | NIST | |
Inp | Outlier 400.00 | NIST | |
Inp | 385.00 | NIST | |
Inp | Outlier 370.00 | NIST | |
Inp | 388.00 | NIST | |
Inp | 386.00 | NIST | |
Inp | 384.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 383.00 | NIST | |
Inp | 387.00 | NIST | |
Inp | 388.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 390.00 | NIST | |
Inp | 383.00 | NIST | |
I | [427.00; 438.00] | ||
I | 438.00 | NIST | |
I | 427.00 | NIST | |
S°gas | 293.59 | J/mol×K | NIST |
S°liquid | 194.00 | J/mol×K | NIST |
Tboil | [266.20; 269.15] | K | |
Tboil | 266.20 | K | KDB |
Tboil | 266.26 | K | NIST |
Tboil | 266.30 | K | NIST |
Tboil | 268.15 ± 1.50 | K | NIST |
Tboil | 267.15 ± 1.50 | K | NIST |
Tboil | Outlier 268.65 ± 1.50 | K | NIST |
Tboil | 266.40 ± 0.50 | K | NIST |
Tboil | 267.15 ± 1.00 | K | NIST |
Tboil | 267.15 ± 1.00 | K | NIST |
Tboil | 266.55 ± 0.70 | K | NIST |
Tboil | 266.35 ± 0.50 | K | NIST |
Tboil | 266.65 ± 2.00 | K | NIST |
Tboil | 266.26 ± 0.55 | K | NIST |
Tboil | 266.55 ± 0.30 | K | NIST |
Tboil | 266.22 ± 0.20 | K | NIST |
Tboil | 267.15 ± 2.00 | K | NIST |
Tboil | 267.15 ± 2.00 | K | NIST |
Tboil | 266.55 ± 1.00 | K | NIST |
Tboil | 266.45 ± 0.50 | K | NIST |
Tboil | 267.15 ± 2.00 | K | NIST |
Tboil | 266.85 ± 1.00 | K | NIST |
Tboil | 266.20 ± 0.50 | K | NIST |
Tboil | 267.15 ± 1.50 | K | NIST |
Tboil | 266.35 ± 0.20 | K | NIST |
Tboil | 266.55 ± 0.50 | K | NIST |
Tboil | 266.55 ± 2.00 | K | NIST |
Tboil | 267.15 ± 2.00 | K | NIST |
Tboil | Outlier 269.15 ± 2.00 | K | NIST |
Tboil | 267.15 ± 2.00 | K | NIST |
Tc | [417.88; 420.15] | K | |
Tc | 417.90 | K | KDB |
Tc | 417.90 ± 0.10 | K | NIST |
Tc | 417.88 ± 0.10 | K | NIST |
Tc | 420.15 ± 2.00 | K | NIST |
Tfus | [125.40; 132.95] | K | |
Tfus | 132.70 | K | KDB |
Tfus | 132.95 | K | Aq. Sol... |
Tfus | 132.38 | K | NIST |
Tfus | 132.45 ± 0.30 | K | NIST |
Tfus | 125.40 ± 0.50 | K | NIST |
Ttriple | 132.40 ± 0.20 | K | NIST |
Vc | [0.239; 0.239] | m3/kmol | |
Vc | 0.239 | m3/kmol | KDB |
Vc | 0.239 | m3/kmol | NIST |
Zc | 0.2751370 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [75.86; 100.25] | J/mol×K | [239.15; 353.15] | |
Cp,gas | 75.86 ± 0.38 | J/mol×K | 239.15 | NIST |
Cp,gas | 82.89 ± 0.41 | J/mol×K | 272.15 | NIST |
Cp,gas | 91.67 ± 0.46 | J/mol×K | 312.15 | NIST |
Cp,gas | 100.25 ± 0.50 | J/mol×K | 353.15 | NIST |
Cp,liquid | [121.30; 121.42] | J/mol×K | [253.10; 266.26] | |
Cp,liquid | 121.42 | J/mol×K | 253.10 | NIST |
Cp,liquid | 121.30 | J/mol×K | 266.26 | NIST |
ΔfusH | [5.92; 5.92] | kJ/mol | [132.40; 132.40] | |
ΔfusH | 5.92 | kJ/mol | 132.40 | NIST |
ΔfusH | 5.92 | kJ/mol | 132.40 | NIST |
ΔfusH | 5.92 | kJ/mol | 132.40 | NIST |
ΔvapH | [22.12; 23.10] | kJ/mol | [244.50; 394.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 22.2 22.4 22.6 22.8 23 250 300 350 | ||||
ΔvapH | 22.80 | kJ/mol | 244.50 | NIST |
ΔvapH | 23.10 | kJ/mol | 245.50 | NIST |
ΔvapH | 22.12 | kJ/mol | 266.30 | KDB |
ΔvapH | 22.70 | kJ/mol | 289.50 | NIST |
ΔvapH | 22.20 | kJ/mol | 343.00 | NIST |
ΔvapH | 22.20 | kJ/mol | 350.50 | NIST |
ΔvapH | 22.30 | kJ/mol | 394.50 | NIST |
Pvap | [133.00; 1546.60] | kPa | [273.15; 364.52] | |
T(K) Vapor pressure (kPa) 0 200 400 600 800 1000 1200 1400 1600 300 350 | ||||
Pvap | 133.00 | kPa | 273.15 | (Vapour... |
Pvap | 133.00 | kPa | 273.15 | Vapor l... |
Pvap | 223.00 | kPa | 288.15 | Vapor-L... |
Pvap | 224.00 | kPa | 288.15 | Vapor l... |
Pvap | 224.00 | kPa | 288.15 | (Vapour... |
Pvap | 353.00 | kPa | 303.15 | Vapor l... |
Pvap | 352.00 | kPa | 303.15 | Vapor-L... |
Pvap | 353.00 | kPa | 303.15 | (Vapour... |
Pvap | 413.70 | kPa | 308.13 | Vapor-L... |
Pvap | 467.10 | kPa | 312.59 | Phase e... |
Pvap | 466.10 | kPa | 312.59 | Vapour ... |
Pvap | 465.30 | kPa | 312.60 | Isother... |
Pvap | 536.00 | kPa | 318.15 | Vapor-L... |
Pvap | 538.00 | kPa | 318.15 | (Vapour... |
Pvap | 538.00 | kPa | 318.15 | Vapor l... |
Pvap | 542.10 | kPa | 318.35 | Vapor-L... |
Pvap | 538.15 | kPa | 318.40 | Vapour ... |
Pvap | 605.14 | kPa | 322.79 | Isother... |
Pvap | 607.94 | kPa | 323.07 | Vapor-L... |
Pvap | 608.94 | kPa | 323.11 | Isother... |
Pvap | 608.84 | kPa | 323.14 | Isother... |
Pvap | 609.14 | kPa | 323.14 | Isother... |
Pvap | 611.04 | kPa | 323.15 | Isother... |
Pvap | 787.00 | kPa | 333.15 | Vapor l... |
Pvap | 785.00 | kPa | 333.15 | Vapor-L... |
Pvap | 787.00 | kPa | 333.15 | (Vapour... |
Pvap | 855.50 | kPa | 336.84 | Vapor-L... |
Pvap | 1054.90 | kPa | 346.14 | Vapor-L... |
Pvap | 1107.00 | kPa | 348.15 | Vapor-L... |
Pvap | 1110.00 | kPa | 348.15 | Vapor l... |
Pvap | 1110.00 | kPa | 348.15 | (Vapour... |
Pvap | 1154.30 | kPa | 350.43 | Vapor-L... |
Pvap | 1515.00 | kPa | 363.15 | Vapor-L... |
Pvap | 1546.00 | kPa | 364.49 | Isother... |
Pvap | 1546.50 | kPa | 364.51 | Isother... |
Pvap | 1546.60 | kPa | 364.51 | Isother... |
Pvap | 1546.20 | kPa | 364.51 | Vapor L... |
Pvap | 1546.30 | kPa | 364.52 | Isother... |
ρl | 594.00 | kg/m3 | 293.00 | KDB |
ΔfusS | 44.71 | J/mol×K | 132.40 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [191.15; 285.02] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.40957e+01 | |||
Coefficient B | -2.26626e+03 | |||
Coefficient C | -2.70260e+01 | |||
Temperature range, min. | 191.15 | |||
Temperature range, max. | 285.02 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 200 250 | ||||
Pvap | 1.33 | kPa | 191.15 | Calculated Property |
Pvap | 3.04 | kPa | 201.58 | Calculated Property |
Pvap | 6.33 | kPa | 212.01 | Calculated Property |
Pvap | 12.16 | kPa | 222.44 | Calculated Property |
Pvap | 21.89 | kPa | 232.87 | Calculated Property |
Pvap | 37.23 | kPa | 243.30 | Calculated Property |
Pvap | 60.29 | kPa | 253.73 | Calculated Property |
Pvap | 93.58 | kPa | 264.16 | Calculated Property |
Pvap | 139.97 | kPa | 274.59 | Calculated Property |
Pvap | 202.66 | kPa | 285.02 | Calculated Property |
Pvap | [6.66e-04; 4013.56] | kPa | [132.81; 417.90] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.75294e+01 | |||
Coefficient B | -4.53316e+03 | |||
Coefficient C | -8.37142e+00 | |||
Coefficient D | 1.22482e-05 | |||
Temperature range, min. | 132.81 | |||
Temperature range, max. | 417.90 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 4000 200 300 400 | ||||
Pvap | 6.66e-04 | kPa | 132.81 | Calculated Property |
Pvap | 0.09 | kPa | 164.49 | Calculated Property |
Pvap | 2.01 | kPa | 196.16 | Calculated Property |
Pvap | 16.84 | kPa | 227.84 | Calculated Property |
Pvap | 77.59 | kPa | 259.52 | Calculated Property |
Pvap | 244.97 | kPa | 291.19 | Calculated Property |
Pvap | 603.20 | kPa | 322.87 | Calculated Property |
Pvap | 1256.40 | kPa | 354.55 | Calculated Property |
Pvap | 2334.76 | kPa | 386.22 | Calculated Property |
Pvap | 4013.56 | kPa | 417.90 | Calculated Property |
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