Property | Value | Unit | Source |
---|---|---|---|
PAff | 953.20 | kJ/mol | NIST |
Tig | 753.15 | K | KDB |
BasG | 921.40 | kJ/mol | NIST |
ΔcH°liquid | -4683.20 ± 0.80 | kJ/mol | NIST |
Tflash,oc | 380.37 | K | KDB |
ΔfH°gas | 200.52 | kJ/mol | NIST |
ΔfH°liquid | 141.22 ± 0.92 | kJ/mol | NIST |
ΔvapH° | [47.45; 59.31] | kJ/mol |
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ΔvapH° | 59.31 ± 0.20 | kJ/mol | NIST |
ΔvapH° | 59.30 | kJ/mol | NIST |
ΔvapH° | 58.10 | kJ/mol | NIST |
ΔvapH° | 47.45 | kJ/mol | NIST |
IE | [8.30; 8.67] | eV |
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IE | 8.63 ± 0.02 | eV | NIST |
IE | 8.62 | eV | NIST |
IE | 8.62 | eV | NIST |
IE | 8.62 | eV | NIST |
IE | 8.67 ± 0.05 | eV | NIST |
IE | Outlier 8.30 | eV | NIST |
IE | 8.62 | eV | NIST |
log10WS | [-1.30; -1.30] |
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|
log10WS | -1.30 | Aq. Sol... | |
log10WS | -1.30 | Estimat... | |
logPoct/wat | 2.235 | Crippen Calculated Property | |
McVol | 104.430 | ml/mol | McGowan Calculated Property |
NFPA Fire | 1 | KDB | |
NFPA Health | 2 | KDB | |
Pc | [4860.00; 5780.00] | kPa |
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Pc | 4860.00 | kPa | KDB |
Pc | 5780.00 ± 303.98 | kPa | NIST |
Inp | [206.00; 1247.70] |
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|
Inp | 1231.00 | NIST | |
Inp | 1246.00 | NIST | |
Inp | 1206.00 | NIST | |
Inp | 1207.00 | NIST | |
Inp | 1231.00 | NIST | |
Inp | 1246.00 | NIST | |
Inp | 1226.00 | NIST | |
Inp | 1226.00 | NIST | |
Inp | 1227.00 | NIST | |
Inp | 1231.00 | NIST | |
Inp | 1233.00 | NIST | |
Inp | 1228.00 | NIST | |
Inp | 1247.70 | NIST | |
Inp | 1247.00 | NIST | |
Inp | 1224.70 | NIST | |
Inp | 1233.00 | NIST | |
Inp | 1237.40 | NIST | |
Inp | 1203.70 | NIST | |
Inp | 1224.70 | NIST | |
Inp | 1233.00 | NIST | |
Inp | 1237.40 | NIST | |
Inp | 1239.00 | NIST | |
Inp | 1230.00 | NIST | |
Inp | 1200.00 | NIST | |
Inp | 1242.00 | NIST | |
Inp | 1240.30 | NIST | |
Inp | 1224.00 | NIST | |
Inp | 1221.60 | NIST | |
Inp | 1221.60 | NIST | |
Inp | 1201.00 | NIST | |
Inp | 1206.00 | NIST | |
Inp | 1199.00 | NIST | |
Inp | 1199.00 | NIST | |
Inp | 1200.00 | NIST | |
Inp | 1203.00 | NIST | |
Inp | 1238.00 | NIST | |
Inp | 1242.00 | NIST | |
Inp | 1205.00 | NIST | |
Inp | 1247.00 | NIST | |
Inp | 1247.00 | NIST | |
Inp | Outlier 210.70 | NIST | |
Inp | Outlier 210.37 | NIST | |
Inp | Outlier 206.00 | NIST | |
Inp | Outlier 210.18 | NIST | |
Inp | Outlier 209.51 | NIST | |
Inp | Outlier 210.32 | NIST | |
Inp | Outlier 210.26 | NIST | |
Inp | Outlier 209.70 | NIST | |
Inp | Outlier 210.17 | NIST | |
Inp | Outlier 210.26 | NIST | |
Inp | 1247.00 | NIST | |
Inp | 1200.00 | NIST | |
Inp | 1221.60 | NIST | |
I | [1892.00; 1942.00] |
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|
I | 1892.00 | NIST | |
I | 1897.00 | NIST | |
I | 1924.00 | NIST | |
I | 1897.00 | NIST | |
I | 1924.00 | NIST | |
I | 1897.00 | NIST | |
I | 1924.00 | NIST | |
I | 1920.00 | NIST | |
I | 1903.00 | NIST | |
I | 1942.00 | NIST | |
I | 1942.00 | NIST | |
S°liquid | [217.10; 219.72] | J/mol×K |
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S°liquid | 219.72 | J/mol×K | NIST |
S°liquid | 219.69 | J/mol×K | NIST |
S°liquid | 217.10 | J/mol×K | NIST |
Tboil | [510.31; 510.85] | K |
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Tboil | 510.31 | K | KDB |
Tboil | 510.85 | K | Vapor P... |
Tc | [782.00; 800.15] | K |
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Tc | 782.00 | K | KDB |
Tc | 782.15 ± 3.00 | K | NIST |
Tc | 800.15 ± 3.00 | K | NIST |
Tc | 793.55 ± 10.00 | K | NIST |
Tfus | [250.55; 258.70] | K |
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Tfus | 258.37 | K | KDB |
Tfus | 258.26 | K | Aq. Sol... |
Tfus | 258.25 ± 0.30 | K | NIST |
Tfus | 258.70 ± 0.20 | K | NIST |
Tfus | 258.15 ± 1.00 | K | NIST |
Tfus | 258.30 ± 0.30 | K | NIST |
Tfus | 257.93 ± 0.05 | K | NIST |
Tfus | 253.65 ± 1.00 | K | NIST |
Tfus | Outlier 250.75 ± 0.60 | K | NIST |
Tfus | 258.21 ± 0.25 | K | NIST |
Tfus | 258.30 ± 0.15 | K | NIST |
Tfus | 257.55 ± 0.50 | K | NIST |
Tfus | 252.05 ± 0.50 | K | NIST |
Tfus | 257.55 ± 0.40 | K | NIST |
Tfus | 258.50 ± 0.30 | K | NIST |
Tfus | 258.45 ± 0.30 | K | NIST |
Tfus | 258.15 ± 2.00 | K | NIST |
Tfus | 254.22 ± 0.15 | K | NIST |
Tfus | 253.65 ± 0.20 | K | NIST |
Tfus | Outlier 250.55 ± 0.60 | K | NIST |
Tfus | 253.70 ± 0.50 | K | NIST |
Ttriple | 258.36 ± 0.00 | K | NIST |
Vc | 0.437 | m3/kmol | KDB |
Zc | 0.3266440 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [164.40; 203.80] | J/mol×K | [283.00; 302.50] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 170 180 190 200 285 290 295 300 | ||||
Cp,liquid | 190.40 | J/mol×K | 283.00 | NIST |
Cp,liquid | 164.40 | J/mol×K | 290.00 | NIST |
Cp,liquid | 203.80 | J/mol×K | 298.00 | NIST |
Cp,liquid | 199.20 | J/mol×K | 298.10 | NIST |
Cp,liquid | 194.89 | J/mol×K | 298.15 | NIST |
Cp,liquid | 194.90 | J/mol×K | 298.15 | NIST |
Cp,liquid | 192.90 | J/mol×K | 302.40 | NIST |
Cp,liquid | 192.90 | J/mol×K | 302.50 | NIST |
ΔfusH | [0.07; 10.80] | kJ/mol | [220.00; 258.40] | ![]() |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 0 2 4 6 8 10 220 230 240 250 | ||||
ΔfusH | 0.07 | kJ/mol | 220.00 | NIST |
ΔfusH | 10.72 | kJ/mol | 257.93 | NIST |
ΔfusH | 10.66 | kJ/mol | 258.40 | NIST |
ΔfusH | 10.80 | kJ/mol | 258.40 | NIST |
ΔfusH | 10.66 | kJ/mol | 258.40 | NIST |
ΔvapH | [46.00; 57.90] | kJ/mol | [428.50; 628.50] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 46 48 50 52 54 56 58 450 500 550 600 | ||||
ΔvapH | 48.40 ± 0.20 | kJ/mol | 428.50 | NIST |
ΔvapH | 46.00 ± 0.30 | kJ/mol | 428.50 | NIST |
ΔvapH | 57.90 ± 0.10 | kJ/mol | 428.50 | NIST |
ΔvapH | 55.50 ± 0.10 | kJ/mol | 428.50 | NIST |
ΔvapH | 53.10 ± 0.10 | kJ/mol | 428.50 | NIST |
ΔvapH | 50.70 ± 0.10 | kJ/mol | 428.50 | NIST |
ΔvapH | 49.20 | kJ/mol | 472.00 | NIST |
ΔvapH | 46.50 | kJ/mol | 560.00 | NIST |
ΔvapH | 46.90 | kJ/mol | 620.50 | NIST |
ΔvapH | 46.10 | kJ/mol | 628.50 | NIST |
Pvap | [135.00; 1166.00] | kPa | [523.15; 653.15] | ![]() |
T(K) Vapor pressure (kPa) 200 400 600 800 1000 1200 550 600 650 | ||||
Pvap | 135.00 | kPa | 523.15 | High-Te... |
Pvap | 245.00 | kPa | 553.15 | High-Te... |
Pvap | 416.00 | kPa | 583.15 | High-Te... |
Pvap | 668.00 | kPa | 613.15 | High-Te... |
Pvap | 955.00 | kPa | 638.15 | High-Te... |
Pvap | 1166.00 | kPa | 653.15 | High-Te... |
ρl | [1089.30; 1095.00] | kg/m3 | [293.00; 298.15] | ![]() |
ρl | 1095.00 | kg/m3 | 293.00 | KDB |
ρl | 1089.30 | kg/m3 | 298.15 | Liquid-... |
ρl | 1089.45 | kg/m3 | 298.15 | Binary ... |
ρl | 1089.45 | kg/m3 | 298.15 | (Liquid... |
ΔfusS | [0.31; 41.79] | J/mol×K | [220.00; 258.40] | ![]() |
ΔfusS | 0.31 | J/mol×K | 220.00 | NIST |
ΔfusS | 41.79 | J/mol×K | 258.40 | NIST |
ΔfusS | 41.27 | J/mol×K | 258.40 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 387.20 | K | 2.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [378.08; 543.79] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.45960e+01 | |||
Coefficient B | -4.38177e+03 | |||
Coefficient C | -7.18450e+01 | |||
Temperature range, min. | 378.08 | |||
Temperature range, max. | 543.79 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 378.08 | Calculated Property |
Pvap | 3.00 | kPa | 396.49 | Calculated Property |
Pvap | 6.19 | kPa | 414.90 | Calculated Property |
Pvap | 11.87 | kPa | 433.32 | Calculated Property |
Pvap | 21.36 | kPa | 451.73 | Calculated Property |
Pvap | 36.41 | kPa | 470.14 | Calculated Property |
Pvap | 59.20 | kPa | 488.55 | Calculated Property |
Pvap | 92.37 | kPa | 506.97 | Calculated Property |
Pvap | 139.02 | kPa | 525.38 | Calculated Property |
Pvap | 202.67 | kPa | 543.79 | Calculated Property |
Pvap | [1.33e-04; 4950.83] | kPa | [258.25; 782.15] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 1.33820e+02 | |||
Coefficient B | -1.23999e+04 | |||
Coefficient C | -1.71511e+01 | |||
Coefficient D | 7.84999e-06 | |||
Temperature range, min. | 258.25 | |||
Temperature range, max. | 782.15 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 400 600 | ||||
Pvap | 1.33e-04 | kPa | 258.25 | Calculated Property |
Pvap | 0.04 | kPa | 316.46 | Calculated Property |
Pvap | 1.21 | kPa | 374.67 | Calculated Property |
Pvap | 12.57 | kPa | 432.88 | Calculated Property |
Pvap | 65.67 | kPa | 491.09 | Calculated Property |
Pvap | 224.65 | kPa | 549.31 | Calculated Property |
Pvap | 589.10 | kPa | 607.52 | Calculated Property |
Pvap | 1307.38 | kPa | 665.73 | Calculated Property |
Pvap | 2619.62 | kPa | 723.94 | Calculated Property |
Pvap | 4950.83 | kPa | 782.15 | Calculated Property |
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