Property | Value | Unit | Source |
---|---|---|---|
ω | 0.1790 | KDB | |
ΔcH°liquid | [-1096.00; -1095.90] | kJ/mol | |
ΔcH°liquid | -1096.00 ± 1.40 | kJ/mol | NIST |
ΔcH°liquid | -1095.90 | kJ/mol | NIST |
EA | 0.10 | eV | NIST |
ΔfG° | 21.39 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [2.00; 2.20] | kJ/mol | |
ΔfH°gas | 2.00 ± 2.00 | kJ/mol | NIST |
ΔfH°gas | 2.20 ± 1.40 | kJ/mol | NIST |
ΔfH°liquid | [-25.00; -24.00] | kJ/mol | |
ΔfH°liquid | -24.00 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | -24.30 ± 1.40 | kJ/mol | NIST |
ΔfH°liquid | -25.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 6.74 | kJ/mol | Joback Calculated Property |
ΔvapH° | [26.48; 26.74] | kJ/mol | |
ΔvapH° | 26.74 | kJ/mol | NIST |
ΔvapH° | 26.74 ± 0.09 | kJ/mol | NIST |
ΔvapH° | 26.48 ± 0.08 | kJ/mol | NIST |
ΔvapH° | 26.48 ± 0.08 | kJ/mol | NIST |
IE | [9.74; 10.00] | eV | |
IE | 9.81 ± 0.04 | eV | NIST |
IE | 9.83 | eV | NIST |
IE | 9.74 | eV | NIST |
IE | 9.86 | eV | NIST |
IE | 9.79 | eV | NIST |
IE | 10.00 | eV | NIST |
IE | 9.99 ± 0.02 | eV | NIST |
IE | 10.00 | eV | NIST |
log10WS | [-1.64; -1.64] | ||
log10WS | -1.64 | Aq. Sol... | |
log10WS | -1.64 | Estimat... | |
logPoct/wat | 1.935 | Crippen Calculated Property | |
McVol | 59.220 | ml/mol | McGowan Calculated Property |
NFPA Fire | 4 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 4680.00 | kPa | KDB |
Inp | [489.00; 522.00] | ||
Inp | 513.00 | NIST | |
Inp | 513.00 | NIST | |
Inp | 517.00 | NIST | |
Inp | 519.00 | NIST | |
Inp | 517.00 | NIST | |
Inp | 521.10 | NIST | |
Inp | 513.00 | NIST | |
Inp | Outlier 489.00 | NIST | |
Inp | 498.00 | NIST | |
Inp | 498.00 | NIST | |
Inp | 512.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 522.00 | NIST | |
Inp | 512.00 | NIST | |
Inp | 511.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 520.00 | NIST | |
Inp | 515.00 | NIST | |
Inp | 513.00 | NIST | |
Inp | 498.00 | NIST | |
Inp | 512.00 | NIST | |
Inp | 521.10 | NIST | |
I | [715.00; 750.44] | ||
I | 744.00 | NIST | |
I | 744.00 | NIST | |
I | 744.91 | NIST | |
I | 750.44 | NIST | |
I | 734.18 | NIST | |
I | 736.00 | NIST | |
I | 736.00 | NIST | |
I | 715.00 | NIST | |
I | 736.00 | NIST | |
I | 744.00 | NIST | |
I | 715.00 | NIST | |
S°liquid | 201.54 | J/mol×K | NIST |
Tboil | [304.20; 304.70] | K | |
Tboil | 304.70 | K | KDB |
Tboil | 304.20 | K | NIST |
Tboil | 304.55 ± 0.20 | K | NIST |
Tboil | 304.70 | K | NIST |
Tc | 489.00 | K | KDB |
Tfus | [150.65; 156.00] | K | |
Tfus | 156.00 | K | KDB |
Tfus | 150.65 | K | Aq. Sol... |
Ttriple | 150.59 ± 0.02 | K | NIST |
Vc | 0.219 | m3/kmol | KDB |
Zc | 0.2520840 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [69.91; 86.80] | J/mol×K | [316.58; 506.91] | |
T(K) Ideal gas heat capacity (J/mol×K) 70 75 80 85 350 400 450 500 | ||||
Cp,gas | 69.91 | J/mol×K | 316.58 | Joback Calculated Property |
Cp,gas | 73.19 | J/mol×K | 348.30 | Joback Calculated Property |
Cp,gas | 76.27 | J/mol×K | 380.02 | Joback Calculated Property |
Cp,gas | 79.17 | J/mol×K | 411.75 | Joback Calculated Property |
Cp,gas | 81.88 | J/mol×K | 443.47 | Joback Calculated Property |
Cp,gas | 84.42 | J/mol×K | 475.19 | Joback Calculated Property |
Cp,gas | 86.80 | J/mol×K | 506.91 | Joback Calculated Property |
Cp,liquid | 111.29 | J/mol×K | 298.15 | NIST |
ΔfusH | [6.51; 6.51] | kJ/mol | [150.59; 150.90] | |
ΔfusH | 6.51 | kJ/mol | 150.59 | NIST |
ΔfusH | 6.51 | kJ/mol | 150.90 | NIST |
ΔfusH | 6.51 | kJ/mol | 150.90 | NIST |
ΔvapH | [26.14; 30.18] | kJ/mol | [275.00; 304.70] | |
ΔvapH | 28.40 | kJ/mol | 275.00 | NIST |
ΔvapH | 26.48 | kJ/mol | 298.15 | NIST |
ΔvapH | 30.18 | kJ/mol | 304.70 | KDB |
ΔvapH | 26.14 | kJ/mol | 304.70 | NIST |
ΔfusS | 43.26 | J/mol×K | 150.59 | NIST |
ΔvapS | 88.80 | J/mol×K | 298.15 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 207.22] | kPa | [222.77; 324.61] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.50904e+01 | |||
Coefficient B | -2.91479e+03 | |||
Coefficient C | -2.58590e+01 | |||
Temperature range, min. | 222.77 | |||
Temperature range, max. | 324.61 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 250 300 | ||||
Pvap | 1.33 | kPa | 222.77 | Calculated Property |
Pvap | 2.98 | kPa | 234.09 | Calculated Property |
Pvap | 6.13 | kPa | 245.40 | Calculated Property |
Pvap | 11.76 | kPa | 256.72 | Calculated Property |
Pvap | 21.21 | kPa | 268.03 | Calculated Property |
Pvap | 36.29 | kPa | 279.35 | Calculated Property |
Pvap | 59.32 | kPa | 290.66 | Calculated Property |
Pvap | 93.14 | kPa | 301.98 | Calculated Property |
Pvap | 141.13 | kPa | 313.29 | Calculated Property |
Pvap | 207.22 | kPa | 324.61 | Calculated Property |
Pvap | [2.14e-04; 4883.28] | kPa | [150.65; 482.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.64762e+01 | |||
Coefficient B | -6.23863e+03 | |||
Coefficient C | -1.27358e+01 | |||
Coefficient D | 1.56756e-05 | |||
Temperature range, min. | 150.65 | |||
Temperature range, max. | 482.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 | ||||
Pvap | 2.14e-04 | kPa | 150.65 | Calculated Property |
Pvap | 0.05 | kPa | 187.47 | Calculated Property |
Pvap | 1.67 | kPa | 224.28 | Calculated Property |
Pvap | 16.08 | kPa | 261.10 | Calculated Property |
Pvap | 79.28 | kPa | 297.92 | Calculated Property |
Pvap | 259.14 | kPa | 334.73 | Calculated Property |
Pvap | 653.79 | kPa | 371.55 | Calculated Property |
Pvap | 1398.81 | kPa | 408.37 | Calculated Property |
Pvap | 2697.36 | kPa | 445.18 | Calculated Property |
Pvap | 4883.28 | kPa | 482.00 | Calculated Property |
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