Property | Value | Unit | Source |
---|---|---|---|
PAff | [871.70; 915.60] | kJ/mol |
![]() |
PAff | 915.60 | kJ/mol | NIST |
PAff | 875.00 | kJ/mol | NIST |
PAff | 871.70 | kJ/mol | NIST |
PAff | 884.30 ± 0.50 | kJ/mol | NIST |
BasG | [841.20; 854.90] | kJ/mol |
![]() |
BasG | 854.90 | kJ/mol | NIST |
BasG | 843.50 | kJ/mol | NIST |
BasG | 841.20 | kJ/mol | NIST |
BasG | 852.90 ± 0.50 | kJ/mol | NIST |
ΔcH°liquid | [-2499.90; -2495.50] | kJ/mol |
![]() |
ΔcH°liquid | -2495.50 ± 5.70 | kJ/mol | NIST |
ΔcH°liquid | -2499.90 ± 2.00 | kJ/mol | NIST |
Cp,liquid | 203.79 | J/mol×K | Molar h... |
ΔfG° | -290.84 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-427.00; -426.00] | kJ/mol |
![]() |
ΔfH°gas | -426.00 ± 5.70 | kJ/mol | NIST |
ΔfH°gas | -427.00 ± 3.00 | kJ/mol | NIST |
ΔfH°liquid | [-505.30; -503.00] | kJ/mol |
![]() |
ΔfH°liquid | -505.30 ± 5.70 | kJ/mol | NIST |
ΔfH°liquid | -503.00 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 14.29 | kJ/mol | Joback Calculated Property |
ΔvapH° | 57.86 | kJ/mol | Joback Calculated Property |
log10WS | -0.02 | Crippen Calculated Property | |
logPoct/wat | -0.249 | Crippen Calculated Property | |
McVol | 78.960 | ml/mol | McGowan Calculated Property |
NFPA Fire | 1 | KDB | |
NFPA Health | 1 | KDB | |
Pc | 6220.00 ± 150.00 | kPa | NIST |
Inp | [900.00; 931.00] |
![]() |
|
Inp | 900.00 | NIST | |
Inp | 931.00 | NIST | |
Inp | 912.40 | NIST | |
Inp | 922.00 | NIST | |
Inp | 900.00 | NIST | |
Inp | 912.40 | NIST | |
Inp | 922.00 | NIST | |
I | [1861.00; 1911.00] |
![]() |
|
I | 1890.00 | NIST | |
I | 1911.00 | NIST | |
I | 1870.00 | NIST | |
I | 1911.00 | NIST | |
I | 1861.00 | NIST | |
S°liquid | 223.40 | J/mol×K | NIST |
Tboil | [501.05; 503.20] | K |
![]() |
Tboil | 501.05 | K | Isobari... |
Tboil | 501.15 | K | Isobari... |
Tboil | 503.20 | K | NIST |
Tboil | 502.88 ± 0.05 | K | NIST |
Tboil | 501.15 ± 2.00 | K | NIST |
Tboil | 503.15 ± 2.00 | K | NIST |
Tboil | 501.15 ± 1.00 | K | NIST |
Tc | [727.00; 728.00] | K |
![]() |
Tc | 728.00 | K | Critica... |
Tc | 727.00 ± 3.00 | K | NIST |
Tfus | [289.40; 355.40] | K |
![]() |
Tfus | 292.80 ± 0.50 | K | NIST |
Tfus | Outlier 355.40 ± 1.00 | K | NIST |
Tfus | 294.05 ± 0.60 | K | NIST |
Tfus | 289.40 ± 1.20 | K | NIST |
Tfus | 292.15 ± 2.00 | K | NIST |
Tfus | 289.90 ± 3.00 | K | NIST |
Tfus | 292.40 ± 0.70 | K | NIST |
Ttriple | [289.90; 293.58] | K |
![]() |
Ttriple | 289.90 ± 0.10 | K | NIST |
Ttriple | 293.58 ± 0.02 | K | NIST |
Ttriple | 293.38 ± 0.10 | K | NIST |
Ttriple | 293.58 ± 0.05 | K | NIST |
Vc | 0.297 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [173.07; 208.17] | J/mol×K | [475.28; 633.81] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 170 180 190 200 210 500 550 600 | ||||
Cp,gas | 173.07 | J/mol×K | 475.28 | Joback Calculated Property |
Cp,gas | 179.49 | J/mol×K | 501.70 | Joback Calculated Property |
Cp,gas | 185.68 | J/mol×K | 528.12 | Joback Calculated Property |
Cp,gas | 191.63 | J/mol×K | 554.54 | Joback Calculated Property |
Cp,gas | 197.36 | J/mol×K | 580.97 | Joback Calculated Property |
Cp,gas | 202.87 | J/mol×K | 607.39 | Joback Calculated Property |
Cp,gas | 208.17 | J/mol×K | 633.81 | Joback Calculated Property |
Cp,liquid | [178.00; 237.38] | J/mol×K | [293.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 180 190 200 210 220 230 240 300 320 340 | ||||
Cp,liquid | 200.39 | J/mol×K | 293.15 | Molar h... |
Cp,liquid | 200.51 | J/mol×K | 293.15 | Heat Ca... |
Cp,liquid | 201.33 | J/mol×K | 294.65 | Heat Ca... |
Cp,liquid | 202.16 | J/mol×K | 296.15 | Heat Ca... |
Cp,liquid | 202.99 | J/mol×K | 297.65 | Heat Ca... |
Cp,liquid | 178.00 | J/mol×K | 297.79 | NIST |
Cp,liquid | 203.27 | J/mol×K | 298.15 | Heat Ca... |
Cp,liquid | 200.10 | J/mol×K | 298.15 | NIST |
Cp,liquid | 203.06 | J/mol×K | 298.15 | Molar h... |
Cp,liquid | 203.82 | J/mol×K | 299.15 | Heat Ca... |
Cp,liquid | 204.67 | J/mol×K | 300.65 | Heat Ca... |
Cp,liquid | 205.51 | J/mol×K | 302.15 | Heat Ca... |
Cp,liquid | 205.82 | J/mol×K | 303.15 | Molar h... |
Cp,liquid | 206.36 | J/mol×K | 303.65 | Heat Ca... |
Cp,liquid | 207.22 | J/mol×K | 305.15 | Heat Ca... |
Cp,liquid | 208.08 | J/mol×K | 306.65 | Heat Ca... |
Cp,liquid | 208.95 | J/mol×K | 308.15 | Heat Ca... |
Cp,liquid | 208.65 | J/mol×K | 308.15 | Molar h... |
Cp,liquid | 209.82 | J/mol×K | 309.65 | Heat Ca... |
Cp,liquid | 210.70 | J/mol×K | 311.15 | Heat Ca... |
Cp,liquid | 211.58 | J/mol×K | 312.65 | Heat Ca... |
Cp,liquid | 211.57 | J/mol×K | 313.15 | Molar h... |
Cp,liquid | 212.47 | J/mol×K | 314.15 | Heat Ca... |
Cp,liquid | 213.36 | J/mol×K | 315.65 | Heat Ca... |
Cp,liquid | 214.26 | J/mol×K | 317.15 | Heat Ca... |
Cp,liquid | 214.55 | J/mol×K | 318.15 | Molar h... |
Cp,liquid | 215.17 | J/mol×K | 318.65 | Heat Ca... |
Cp,liquid | 216.08 | J/mol×K | 320.15 | Heat Ca... |
Cp,liquid | 216.99 | J/mol×K | 321.65 | Heat Ca... |
Cp,liquid | 217.91 | J/mol×K | 323.15 | Heat Ca... |
Cp,liquid | 217.61 | J/mol×K | 323.15 | Molar h... |
Cp,liquid | 218.83 | J/mol×K | 324.65 | Heat Ca... |
Cp,liquid | 219.76 | J/mol×K | 326.15 | Heat Ca... |
Cp,liquid | 220.70 | J/mol×K | 327.65 | Heat Ca... |
Cp,liquid | 220.72 | J/mol×K | 328.15 | Molar h... |
Cp,liquid | 221.64 | J/mol×K | 329.15 | Heat Ca... |
Cp,liquid | 222.58 | J/mol×K | 330.65 | Heat Ca... |
Cp,liquid | 223.53 | J/mol×K | 332.15 | Heat Ca... |
Cp,liquid | 223.90 | J/mol×K | 333.15 | Molar h... |
Cp,liquid | 224.49 | J/mol×K | 333.65 | Heat Ca... |
Cp,liquid | 225.45 | J/mol×K | 335.15 | Heat Ca... |
Cp,liquid | 226.41 | J/mol×K | 336.65 | Heat Ca... |
Cp,liquid | 227.12 | J/mol×K | 338.15 | Molar h... |
Cp,liquid | 227.38 | J/mol×K | 338.15 | Heat Ca... |
Cp,liquid | 228.36 | J/mol×K | 339.65 | Heat Ca... |
Cp,liquid | 229.34 | J/mol×K | 341.15 | Heat Ca... |
Cp,liquid | 230.33 | J/mol×K | 342.65 | Heat Ca... |
Cp,liquid | 230.40 | J/mol×K | 343.15 | Molar h... |
Cp,liquid | 231.32 | J/mol×K | 344.15 | Heat Ca... |
Cp,liquid | 232.32 | J/mol×K | 345.65 | Heat Ca... |
Cp,liquid | 233.32 | J/mol×K | 347.15 | Heat Ca... |
Cp,liquid | 233.72 | J/mol×K | 348.15 | Molar h... |
Cp,liquid | 234.32 | J/mol×K | 348.65 | Heat Ca... |
Cp,liquid | 235.34 | J/mol×K | 350.15 | Heat Ca... |
Cp,liquid | 236.35 | J/mol×K | 351.65 | Heat Ca... |
Cp,liquid | 237.38 | J/mol×K | 353.15 | Heat Ca... |
Cp,liquid | 237.07 | J/mol×K | 353.15 | Molar h... |
η | [0.0290542; 0.0972620] | Pa×s | [293.15; 318.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0.03 0.04 0.05 0.06 0.07 0.08 0.09 0.1 300 310 | ||||
η | 0.0972620 | Pa×s | 293.15 | Molecul... |
η | 0.0727454 | Pa×s | 298.15 | Molecul... |
η | 0.0568860 | Pa×s | 303.15 | Molecul... |
η | 0.0448850 | Pa×s | 308.15 | Molecul... |
η | 0.0358106 | Pa×s | 313.15 | Molecul... |
η | 0.0290542 | Pa×s | 318.15 | Molecul... |
ΔfusH | [18.70; 18.70] | kJ/mol | [293.58; 293.60] | ![]() |
ΔfusH | 18.70 | kJ/mol | 293.58 | NIST |
ΔfusH | 18.70 | kJ/mol | 293.60 | NIST |
ΔfusH | 18.70 | kJ/mol | 293.60 | NIST |
ΔvapH | [72.00; 77.10] | kJ/mol | [298.15; 445.00] | ![]() |
ΔvapH | 77.10 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 77.00 ± 2.00 | kJ/mol | 419.00 | NIST |
ΔvapH | 72.00 | kJ/mol | 445.00 | NIST |
Pvap | [0.01; 0.66] | kPa | [329.20; 383.15] | ![]() |
T(K) Vapor pressure (kPa) 0 0.1 0.2 0.3 0.4 0.5 0.6 0.7 340 360 380 | ||||
Pvap | 0.01 | kPa | 329.20 | Thermod... |
Pvap | 0.02 | kPa | 332.30 | Thermod... |
Pvap | 0.02 | kPa | 335.20 | Thermod... |
Pvap | 0.03 | kPa | 338.20 | Thermod... |
Pvap | 0.04 | kPa | 339.60 | Thermod... |
Pvap | 0.04 | kPa | 339.60 | Thermod... |
Pvap | 0.04 | kPa | 341.20 | Thermod... |
Pvap | 0.05 | kPa | 343.20 | Thermod... |
Pvap | 0.05 | kPa | 343.60 | Thermod... |
Pvap | 0.05 | kPa | 343.60 | Thermod... |
Pvap | 0.06 | kPa | 346.30 | Thermod... |
Pvap | 0.07 | kPa | 348.20 | Thermod... |
Pvap | 0.07 | kPa | 348.60 | Thermod... |
Pvap | 0.07 | kPa | 348.60 | Thermod... |
Pvap | 0.08 | kPa | 351.20 | Thermod... |
Pvap | 0.10 | kPa | 353.20 | Thermod... |
Pvap | 0.10 | kPa | 353.60 | Thermod... |
Pvap | 0.10 | kPa | 353.60 | Thermod... |
Pvap | 0.12 | kPa | 356.20 | Thermod... |
Pvap | 0.14 | kPa | 358.30 | Thermod... |
Pvap | 0.14 | kPa | 358.60 | Thermod... |
Pvap | 0.14 | kPa | 358.60 | Thermod... |
Pvap | 0.17 | kPa | 361.20 | Thermod... |
Pvap | 0.19 | kPa | 363.20 | Thermod... |
Pvap | 0.66 | kPa | 383.15 | Vapor-L... |
n0 | [1.43520; 1.44570] | [293.15; 318.20] | ![]() |
|
T(K) Refractive Index 1.44 1.44 1.44 1.44 1.44 1.45 300 310 | ||||
n0 | 1.44510 | 293.15 | Refract... | |
n0 | 1.44310 | 298.15 | Refract... | |
n0 | 1.44420 | 298.15 | Densiti... | |
n0 | 1.44470 | 298.15 | The eff... | |
n0 | 1.44570 | 298.20 | A therm... | |
n0 | 1.44110 | 303.15 | Refract... | |
n0 | 1.43910 | 308.15 | Refract... | |
n0 | 1.44220 | 308.20 | A therm... | |
n0 | 1.44170 | 308.20 | A therm... | |
n0 | 1.43720 | 313.15 | Refract... | |
n0 | 1.43520 | 318.15 | Refract... | |
n0 | 1.43860 | 318.20 | A therm... | |
ρl | [972.71; 1022.21] | kg/m3 | [283.15; 363.15] | ![]() |
T(K) Liquid Density (kg/m3) 970 980 990 1000 1010 1020 300 320 340 360 | ||||
ρl | 1022.21 | kg/m3 | 283.15 | Excess ... |
ρl | 1015.76 | kg/m3 | 293.15 | Excess ... |
ρl | 1016.11 | kg/m3 | 293.15 | Excess ... |
ρl | 1016.37 | kg/m3 | 293.15 | Densiti... |
ρl | 1013.04 | kg/m3 | 298.15 | Densiti... |
ρl | 1012.68 | kg/m3 | 298.15 | Excess ... |
ρl | 1012.60 | kg/m3 | 298.15 | Densiti... |
ρl | 1013.06 | kg/m3 | 298.15 | Excess ... |
ρl | 1013.90 | kg/m3 | 298.15 | Investi... |
ρl | 1012.80 | kg/m3 | 298.15 | Acousti... |
ρl | 1012.96 | kg/m3 | 298.15 | Isobari... |
ρl | 1013.04 | kg/m3 | 298.15 | Isobari... |
ρl | 1009.96 | kg/m3 | 303.15 | Densiti... |
ρl | 1009.99 | kg/m3 | 303.15 | Excess ... |
ρl | 1010.60 | kg/m3 | 303.15 | Investi... |
ρl | 1009.60 | kg/m3 | 303.15 | Densiti... |
ρl | 1009.77 | kg/m3 | 303.15 | Acousti... |
ρl | 1009.54 | kg/m3 | 303.15 | Excess ... |
ρl | 1007.50 | kg/m3 | 308.15 | Investi... |
ρl | 1003.95 | kg/m3 | 308.15 | Effect ... |
ρl | 1003.95 | kg/m3 | 308.15 | Thermod... |
ρl | 1003.95 | kg/m3 | 308.15 | A compa... |
ρl | 1003.95 | kg/m3 | 308.15 | Effect ... |
ρl | 1006.75 | kg/m3 | 308.15 | Densiti... |
ρl | 1006.70 | kg/m3 | 308.15 | Densiti... |
ρl | 1006.43 | kg/m3 | 308.15 | Excess ... |
ρl | 1006.74 | kg/m3 | 308.15 | Acousti... |
ρl | 1003.70 | kg/m3 | 313.15 | Acousti... |
ρl | 1003.70 | kg/m3 | 313.15 | Densiti... |
ρl | 1003.85 | kg/m3 | 313.15 | Excess ... |
ρl | 1003.37 | kg/m3 | 313.15 | Excess ... |
ρl | 1003.55 | kg/m3 | 313.15 | Densiti... |
ρl | 1000.72 | kg/m3 | 318.15 | Densiti... |
ρl | 1000.45 | kg/m3 | 318.15 | Excess ... |
ρl | 1000.67 | kg/m3 | 318.15 | Acousti... |
ρl | 997.80 | kg/m3 | 323.15 | Densiti... |
ρl | 997.14 | kg/m3 | 323.15 | Excess ... |
ρl | 997.63 | kg/m3 | 323.15 | Acousti... |
ρl | 994.02 | kg/m3 | 328.15 | Excess ... |
ρl | 994.41 | kg/m3 | 328.15 | Densiti... |
ρl | 990.93 | kg/m3 | 333.15 | Excess ... |
ρl | 987.93 | kg/m3 | 338.15 | Excess ... |
ρl | 984.81 | kg/m3 | 343.15 | Excess ... |
ρl | 981.70 | kg/m3 | 348.15 | Excess ... |
ρl | 978.59 | kg/m3 | 353.15 | Excess ... |
ρl | 972.71 | kg/m3 | 363.15 | Excess ... |
ΔfusS | 63.72 | J/mol×K | 293.58 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 393.20 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [387.92; 530.19] |
The Yaw...
![]() |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.61683e+01 | |||
Coefficient B | -4.88254e+03 | |||
Coefficient C | -8.04700e+01 | |||
Temperature range, min. | 387.92 | |||
Temperature range, max. | 530.19 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 387.92 | Calculated Property |
Pvap | 2.90 | kPa | 403.73 | Calculated Property |
Pvap | 5.86 | kPa | 419.54 | Calculated Property |
Pvap | 11.13 | kPa | 435.34 | Calculated Property |
Pvap | 20.02 | kPa | 451.15 | Calculated Property |
Pvap | 34.30 | kPa | 466.96 | Calculated Property |
Pvap | 56.36 | kPa | 482.77 | Calculated Property |
Pvap | 89.17 | kPa | 498.57 | Calculated Property |
Pvap | 136.45 | kPa | 514.38 | Calculated Property |
Pvap | 202.65 | kPa | 530.19 | Calculated Property |
Pvap | [8.47e-04; 4890.03] | kPa | [293.05; 667.00] |
KDB Vap...
![]() |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 5.07189e+01 | |||
Coefficient B | -9.72020e+03 | |||
Coefficient C | -4.35830e+00 | |||
Coefficient D | 1.55136e-06 | |||
Temperature range, min. | 293.05 | |||
Temperature range, max. | 667.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 600 | ||||
Pvap | 8.47e-04 | kPa | 293.05 | Calculated Property |
Pvap | 0.03 | kPa | 334.60 | Calculated Property |
Pvap | 0.47 | kPa | 376.15 | Calculated Property |
Pvap | 4.13 | kPa | 417.70 | Calculated Property |
Pvap | 23.71 | kPa | 459.25 | Calculated Property |
Pvap | 100.14 | kPa | 500.80 | Calculated Property |
Pvap | 334.75 | kPa | 542.35 | Calculated Property |
Pvap | 934.11 | kPa | 583.90 | Calculated Property |
Pvap | 2261.64 | kPa | 625.45 | Calculated Property |
Pvap | 4890.03 | kPa | 667.00 | Calculated Property |
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