Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3060 | KDB | |
PAff | 943.40 | kJ/mol | NIST |
BasG | 911.60 | kJ/mol | NIST |
ΔcH°liquid | [-3429.80; -3300.40] | kJ/mol |
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ΔcH°liquid | -3300.40 ± 1.30 | kJ/mol | NIST |
ΔcH°liquid | -3423.20 ± 0.50 | kJ/mol | NIST |
ΔcH°liquid | -3429.80 ± 1.00 | kJ/mol | NIST |
ΔcH°liquid | -3402.00 | kJ/mol | NIST |
μ | 2.40 | debye | KDB |
ΔfG° | 184.40 | kJ/mol | KDB |
ΔfH°gas | [75.50; 113.60] | kJ/mol |
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ΔfH°gas | 106.20 | kJ/mol | KDB |
ΔfH°gas | 103.60 ± 1.30 | kJ/mol | NIST |
ΔfH°gas | 106.10 ± 0.71 | kJ/mol | NIST |
ΔfH°gas | 113.60 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | 113.60 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | Outlier 75.50 | kJ/mol | NIST |
ΔfH°liquid | [33.00; 68.30] | kJ/mol |
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ΔfH°liquid | 61.10 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | 61.71 ± 0.59 | kJ/mol | NIST |
ΔfH°liquid | 68.30 ± 1.00 | kJ/mol | NIST |
ΔfH°liquid | 33.00 | kJ/mol | NIST |
ΔvapH° | [42.50; 45.30] | kJ/mol |
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ΔvapH° | 44.57 | kJ/mol | NIST |
ΔvapH° | 44.50 ± 2.00 | kJ/mol | NIST |
ΔvapH° | 42.50 ± 0.30 | kJ/mol | NIST |
ΔvapH° | 42.50 | kJ/mol | NIST |
ΔvapH° | 44.64 | kJ/mol | NIST |
ΔvapH° | 44.60 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 44.43 | kJ/mol | NIST |
ΔvapH° | 44.40 | kJ/mol | NIST |
ΔvapH° | 45.23 | kJ/mol | NIST |
ΔvapH° | 45.30 | kJ/mol | NIST |
IE | [8.90; 9.43] | eV |
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IE | 9.00 | eV | NIST |
IE | 8.90 | eV | NIST |
IE | 9.43 ± 0.05 | eV | NIST |
IE | 9.40 ± 0.10 | eV | NIST |
IE | 9.04 ± 0.03 | eV | NIST |
IE | 9.30 | eV | NIST |
IE | 9.31 | eV | NIST |
IE | 9.29 | eV | NIST |
log10WS | -1.71 | Crippen Calculated Property | |
logPoct/wat | 1.390 | Crippen Calculated Property | |
McVol | 81.620 | ml/mol | McGowan Calculated Property |
Pc | 4480.00 | kPa | KDB |
Inp | [133.54; 877.00] |
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|
Inp | 844.90 | NIST | |
Inp | 852.00 | NIST | |
Inp | 877.00 | NIST | |
Inp | 843.40 | NIST | |
Inp | 846.00 | NIST | |
Inp | 857.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | 859.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 826.80 | NIST | |
Inp | 856.00 | NIST | |
Inp | 863.00 | NIST | |
Inp | 871.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 849.00 | NIST | |
Inp | 849.00 | NIST | |
Inp | 869.00 | NIST | |
Inp | 838.00 | NIST | |
Inp | 860.00 | NIST | |
Inp | 831.00 | NIST | |
Inp | 852.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 861.00 | NIST | |
Inp | 857.00 | NIST | |
Inp | 868.00 | NIST | |
Inp | 859.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 863.00 | NIST | |
Inp | 874.00 | NIST | |
Inp | 866.40 | NIST | |
Inp | 864.00 | NIST | |
Inp | 864.00 | NIST | |
Inp | 845.00 | NIST | |
Inp | 850.00 | NIST | |
Inp | 868.00 | NIST | |
Inp | 841.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 871.00 | NIST | |
Inp | 872.00 | NIST | |
Inp | 834.00 | NIST | |
Inp | 835.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | 832.00 | NIST | |
Inp | Outlier 133.54 | NIST | |
Inp | Outlier 133.54 | NIST | |
I | [1264.00; 1347.00] |
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|
I | 1310.00 | NIST | |
I | 1303.00 | NIST | |
I | 1284.00 | NIST | |
I | 1297.00 | NIST | |
I | 1302.00 | NIST | |
I | 1289.00 | NIST | |
I | Outlier 1347.00 | NIST | |
I | 1289.00 | NIST | |
I | 1290.00 | NIST | |
I | 1290.00 | NIST | |
I | 1292.00 | NIST | |
I | 1319.00 | NIST | |
I | 1291.00 | NIST | |
I | 1290.00 | NIST | |
I | 1303.00 | NIST | |
I | 1304.00 | NIST | |
I | 1304.00 | NIST | |
I | 1298.00 | NIST | |
I | 1284.00 | NIST | |
I | 1284.00 | NIST | |
I | 1306.00 | NIST | |
I | 1305.00 | NIST | |
I | Outlier 1338.00 | NIST | |
I | 1323.00 | NIST | |
I | 1292.00 | NIST | |
I | 1289.00 | NIST | |
I | 1292.00 | NIST | |
I | Outlier 1264.00 | NIST | |
I | 1291.00 | NIST | |
I | 1288.00 | NIST | |
I | 1301.00 | NIST | |
I | 1319.00 | NIST | |
I | 1305.00 | NIST | |
I | 1305.00 | NIST | |
I | 1311.00 | NIST | |
I | 1283.00 | NIST | |
I | 1285.00 | NIST | |
I | 1286.00 | NIST | |
I | 1287.00 | NIST | |
I | 1287.00 | NIST | |
I | 1287.00 | NIST | |
I | 1288.00 | NIST | |
I | 1288.00 | NIST | |
I | 1310.00 | NIST | |
I | 1289.00 | NIST | |
S°liquid | 216.31 | J/mol×K | NIST |
Tboil | 417.29 | K | KDB |
Tc | [644.85; 645.00] | K |
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Tc | 645.00 | K | KDB |
Tc | 645.00 | K | NIST |
Tc | 644.85 ± 0.50 | K | NIST |
Tfus | [251.95; 255.45] | K |
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Tfus | 255.01 | K | KDB |
Tfus | 254.85 ± 0.50 | K | NIST |
Tfus | 255.15 ± 1.00 | K | NIST |
Tfus | 254.95 ± 0.06 | K | NIST |
Tfus | 254.63 ± 0.35 | K | NIST |
Tfus | 255.25 ± 0.20 | K | NIST |
Tfus | Outlier 251.95 ± 0.70 | K | NIST |
Tfus | 255.45 ± 0.30 | K | NIST |
Tfus | 254.85 ± 0.30 | K | NIST |
Ttriple | [255.01; 255.01] | K |
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Ttriple | 255.01 | K | KDB |
Ttriple | 255.01 ± 0.06 | K | NIST |
Vc | 0.288 | m3/kmol | KDB |
Zc | 0.2405880 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,liquid | [156.05; 160.83] | J/mol×K | [293.15; 303.15] | ![]() |
Cp,liquid | 156.05 | J/mol×K | 293.15 | Excess ... |
Cp,liquid | 158.75 | J/mol×K | 298.15 | Excess ... |
Cp,liquid | 158.69 | J/mol×K | 298.15 | NIST |
Cp,liquid | 160.83 | J/mol×K | 303.15 | Excess ... |
η | [0.0005390; 0.0009459] | Pa×s | [293.15; 343.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 300 320 340 | ||||
η | 0.0009459 | Pa×s | 293.15 | Density... |
η | 0.0009459 | Pa×s | 293.15 | Densiti... |
η | 0.0008318 | Pa×s | 303.15 | Density... |
η | 0.0008318 | Pa×s | 303.15 | Densiti... |
η | 0.0007352 | Pa×s | 313.15 | Density... |
η | 0.0007352 | Pa×s | 313.15 | Densiti... |
η | 0.0006565 | Pa×s | 323.15 | Density... |
η | 0.0006565 | Pa×s | 323.15 | Densiti... |
η | 0.0005936 | Pa×s | 333.15 | Density... |
η | 0.0005936 | Pa×s | 333.15 | Densiti... |
η | 0.0005390 | Pa×s | 343.15 | Density... |
η | 0.0005390 | Pa×s | 343.15 | Densiti... |
ΔfusH | [14.18; 14.18] | kJ/mol | [255.00; 255.01] | ![]() |
ΔfusH | 14.18 | kJ/mol | 255.00 | NIST |
ΔfusH | 14.18 | kJ/mol | 255.00 | NIST |
ΔfusH | 14.18 | kJ/mol | 255.01 | NIST |
ΔsubH | 62.20 | kJ/mol | 240.00 | NIST |
ΔvapH | [36.10; 43.60] | kJ/mol | [313.00; 603.00] | ![]() |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 400 500 600 | ||||
ΔvapH | 43.60 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 42.70 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 42.00 ± 0.10 | kJ/mol | 343.00 | NIST |
ΔvapH | 40.40 ± 0.10 | kJ/mol | 368.00 | NIST |
ΔvapH | 40.20 ± 0.10 | kJ/mol | 372.00 | NIST |
ΔvapH | 40.90 ± 0.10 | kJ/mol | 385.50 | NIST |
ΔvapH | 38.60 ± 0.10 | kJ/mol | 385.50 | NIST |
ΔvapH | 43.20 ± 0.10 | kJ/mol | 385.50 | NIST |
ΔvapH | 36.10 ± 0.20 | kJ/mol | 385.50 | NIST |
ΔvapH | 41.00 | kJ/mol | 386.00 | NIST |
ΔvapH | 38.90 ± 0.10 | kJ/mol | 393.00 | NIST |
ΔvapH | 41.30 | kJ/mol | 402.50 | NIST |
ΔvapH | 41.30 | kJ/mol | 402.50 | NIST |
ΔvapH | 40.10 | kJ/mol | 416.00 | NIST |
ΔvapH | 37.40 ± 0.10 | kJ/mol | 417.00 | NIST |
ΔvapH | 37.35 | kJ/mol | 417.30 | NIST |
ΔvapH | 37.70 | kJ/mol | 510.00 | NIST |
ΔvapH | 36.80 | kJ/mol | 603.00 | NIST |
ρl | [942.83; 961.00] | kg/m3 | [288.00; 308.15] | ![]() |
T(K) Liquid Density (kg/m3) 945 950 955 960 290 295 300 305 | ||||
ρl | 961.00 | kg/m3 | 288.00 | KDB |
ρl | 956.58 | kg/m3 | 293.15 | Thermod... |
ρl | 952.00 | kg/m3 | 298.15 | Thermod... |
ρl | 952.00 | kg/m3 | 298.15 | Thermod... |
ρl | 952.61 | kg/m3 | 298.15 | Determi... |
ρl | 952.00 | kg/m3 | 298.15 | Thermod... |
ρl | 947.45 | kg/m3 | 303.15 | Thermod... |
ρl | 942.83 | kg/m3 | 308.15 | Thermod... |
ΔfusS | 55.61 | J/mol×K | 255.01 | NIST |
csound,fluid | [1384.03; 1445.91] | m/s | [293.15; 308.15] | ![]() |
T(K) Speed of sound in fluid (m/s) 1380 1390 1400 1410 1420 1430 1440 1450 295 300 305 | ||||
csound,fluid | 1445.91 | m/s | 293.15 | Topolog... |
csound,fluid | 1424.01 | m/s | 298.15 | Topolog... |
csound,fluid | 1424.01 | m/s | 298.15 | Thermod... |
csound,fluid | 1404.05 | m/s | 303.15 | Topolog... |
csound,fluid | 1404.05 | m/s | 303.15 | Thermod... |
csound,fluid | 1384.03 | m/s | 308.15 | Topolog... |
csound,fluid | 1384.03 | m/s | 308.15 | Thermod... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [306.29; 444.55] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43698e+01 | |||
Coefficient B | -3.51056e+03 | |||
Coefficient C | -5.69960e+01 | |||
Temperature range, min. | 306.29 | |||
Temperature range, max. | 444.55 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 | ||||
Pvap | 1.33 | kPa | 306.29 | Calculated Property |
Pvap | 3.02 | kPa | 321.65 | Calculated Property |
Pvap | 6.25 | kPa | 337.01 | Calculated Property |
Pvap | 12.00 | kPa | 352.38 | Calculated Property |
Pvap | 21.59 | kPa | 367.74 | Calculated Property |
Pvap | 36.77 | kPa | 383.10 | Calculated Property |
Pvap | 59.68 | kPa | 398.46 | Calculated Property |
Pvap | 92.90 | kPa | 413.83 | Calculated Property |
Pvap | 139.44 | kPa | 429.19 | Calculated Property |
Pvap | 202.66 | kPa | 444.55 | Calculated Property |
Pvap | [0.04; 4395.51] | kPa | [255.01; 645.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.64539e+01 | |||
Coefficient B | -7.79454e+03 | |||
Coefficient C | -8.93688e+00 | |||
Coefficient D | 4.40804e-06 | |||
Temperature range, min. | 255.01 | |||
Temperature range, max. | 645.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 600 | ||||
Pvap | 0.04 | kPa | 255.01 | Calculated Property |
Pvap | 0.82 | kPa | 298.34 | Calculated Property |
Pvap | 7.53 | kPa | 341.67 | Calculated Property |
Pvap | 38.81 | kPa | 385.01 | Calculated Property |
Pvap | 135.48 | kPa | 428.34 | Calculated Property |
Pvap | 361.88 | kPa | 471.67 | Calculated Property |
Pvap | 800.10 | kPa | 515.00 | Calculated Property |
Pvap | 1544.39 | kPa | 558.34 | Calculated Property |
Pvap | 2701.05 | kPa | 601.67 | Calculated Property |
Pvap | 4395.51 | kPa | 645.00 | Calculated Property |
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