Property | Value | Unit | Source |
---|---|---|---|
ω | 0.4800 | KDB | |
ΔfG° | 162.57 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -54.48 | kJ/mol | Joback Calculated Property |
ΔfusH° | 20.88 | kJ/mol | Joback Calculated Property |
ΔvapH° | [60.00; 60.20] | kJ/mol |
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ΔvapH° | 60.20 | kJ/mol | NIST |
ΔvapH° | 60.00 | kJ/mol | NIST |
log10WS | [-5.21; -5.21] |
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|
log10WS | -5.21 | Aq. Sol... | |
log10WS | -5.21 | Estimat... | |
logPoct/wat | 3.809 | Crippen Calculated Property | |
McVol | 156.180 | ml/mol | McGowan Calculated Property |
Pc | 2380.00 | kPa | KDB |
Inp | [213.10; 1277.00] |
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|
Inp | 1255.00 | NIST | |
Inp | 1239.00 | NIST | |
Inp | 1260.00 | NIST | |
Inp | 1271.00 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1230.00 | NIST | |
Inp | 1264.00 | NIST | |
Inp | 1263.00 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1250.00 | NIST | |
Inp | 1256.00 | NIST | |
Inp | 1225.40 | NIST | |
Inp | 1228.80 | NIST | |
Inp | 1243.60 | NIST | |
Inp | 1249.70 | NIST | |
Inp | 1256.20 | NIST | |
Inp | 1225.40 | NIST | |
Inp | 1228.80 | NIST | |
Inp | 1228.00 | NIST | |
Inp | 1231.00 | NIST | |
Inp | 1259.00 | NIST | |
Inp | 1277.00 | NIST | |
Inp | 1273.00 | NIST | |
Inp | 1223.00 | NIST | |
Inp | 1231.20 | NIST | |
Inp | 1235.00 | NIST | |
Inp | 1239.70 | NIST | |
Inp | 1245.00 | NIST | |
Inp | 1245.00 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1252.75 | NIST | |
Inp | 1254.60 | NIST | |
Inp | 1258.40 | NIST | |
Inp | 1260.90 | NIST | |
Inp | 1233.00 | NIST | |
Inp | 1245.20 | NIST | |
Inp | 1247.20 | NIST | |
Inp | 1247.30 | NIST | |
Inp | 1254.60 | NIST | |
Inp | 1258.40 | NIST | |
Inp | 1260.90 | NIST | |
Inp | 1257.00 | NIST | |
Inp | 1254.00 | NIST | |
Inp | 1247.00 | NIST | |
Inp | 1241.23 | NIST | |
Inp | 1245.30 | NIST | |
Inp | 1248.08 | NIST | |
Inp | 1259.18 | NIST | |
Inp | 1263.43 | NIST | |
Inp | 1266.48 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1246.00 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1256.00 | NIST | |
Inp | 1220.00 | NIST | |
Inp | 1262.00 | NIST | |
Inp | 1254.00 | NIST | |
Inp | 1242.00 | NIST | |
Inp | 1267.20 | NIST | |
Inp | 1244.00 | NIST | |
Inp | 1228.00 | NIST | |
Inp | Outlier 213.10 | NIST | |
Inp | 1254.60 | NIST | |
Inp | 1247.20 | NIST | |
Inp | 1257.00 | NIST | |
Inp | 1248.08 | NIST | |
Inp | 1245.00 | NIST | |
Inp | 1228.00 | NIST | |
Inp | 1255.00 | NIST | |
Inp | 1230.00 | NIST | |
Inp | 1256.00 | NIST | |
Inp | 1256.20 | NIST | |
Inp | 1259.00 | NIST | |
Inp | 1235.00 | NIST | |
I | [1489.20; 1578.90] |
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|
I | 1556.10 | NIST | |
I | 1561.80 | NIST | |
I | 1567.50 | NIST | |
I | 1573.20 | NIST | |
I | 1578.90 | NIST | |
I | 1489.20 | NIST | |
I | 1531.00 | NIST | |
I | 1529.00 | NIST | |
I | 1499.00 | NIST | |
I | 1515.00 | NIST | |
I | 1513.00 | NIST | |
I | 1513.00 | NIST | |
I | 1524.00 | NIST | |
I | 1537.00 | NIST | |
I | 1551.00 | NIST | |
I | 1500.00 | NIST | |
I | 1532.00 | NIST | |
I | 1531.00 | NIST | |
Tboil | [481.00; 500.50] | K |
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Tboil | 499.30 | K | KDB |
Tboil | 499.30 | K | NIST |
Tboil | 498.92 ± 0.20 | K | NIST |
Tboil | 498.92 ± 0.50 | K | NIST |
Tboil | 488.65 ± 1.50 | K | NIST |
Tboil | 498.15 ± 1.50 | K | NIST |
Tboil | 490.00 ± 10.00 | K | NIST |
Tboil | 498.90 ± 0.50 | K | NIST |
Tboil | 491.00 ± 12.00 | K | NIST |
Tboil | 485.00 ± 6.00 | K | NIST |
Tboil | 487.00 ± 20.00 | K | NIST |
Tboil | 494.00 ± 3.00 | K | NIST |
Tboil | 500.00 ± 4.00 | K | NIST |
Tboil | 500.00 ± 4.00 | K | NIST |
Tboil | 500.00 ± 5.00 | K | NIST |
Tboil | 499.00 ± 6.00 | K | NIST |
Tboil | 492.00 ± 5.00 | K | NIST |
Tboil | 492.00 ± 5.00 | K | NIST |
Tboil | 494.00 ± 6.00 | K | NIST |
Tboil | 500.50 ± 1.00 | K | NIST |
Tboil | 488.15 ± 2.00 | K | NIST |
Tboil | 488.00 ± 5.00 | K | NIST |
Tboil | 493.00 ± 5.00 | K | NIST |
Tboil | Outlier 481.00 ± 6.00 | K | NIST |
Tc | 697.50 | K | KDB |
Tfus | [206.40; 212.00] | K |
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Tfus | 212.00 | K | KDB |
Tfus | 209.70 ± 0.30 | K | NIST |
Tfus | 209.70 ± 0.50 | K | NIST |
Tfus | 206.40 ± 1.50 | K | NIST |
Vc | 0.620 | m3/kmol | KDB |
Zc | 0.2544410 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [345.46; 433.87] | J/mol×K | [500.64; 699.90] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 340 360 380 400 420 440 500 600 700 | ||||
Cp,gas | 345.46 | J/mol×K | 500.64 | Joback Calculated Property |
Cp,gas | 362.33 | J/mol×K | 533.85 | Joback Calculated Property |
Cp,gas | 378.30 | J/mol×K | 567.06 | Joback Calculated Property |
Cp,gas | 393.41 | J/mol×K | 600.27 | Joback Calculated Property |
Cp,gas | 407.68 | J/mol×K | 633.48 | Joback Calculated Property |
Cp,gas | 421.16 | J/mol×K | 666.69 | Joback Calculated Property |
Cp,gas | 433.87 | J/mol×K | 699.90 | Joback Calculated Property |
Cp,liquid | 248.00 | J/mol×K | 293.00 | NIST |
η | [0.0002074; 0.0038377] | Pa×s | [251.42; 500.64] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 300 400 500 | ||||
η | 0.0038377 | Pa×s | 251.42 | Joback Calculated Property |
η | 0.0016716 | Pa×s | 292.96 | Joback Calculated Property |
η | 0.0008950 | Pa×s | 334.49 | Joback Calculated Property |
η | 0.0005501 | Pa×s | 376.03 | Joback Calculated Property |
η | 0.0003725 | Pa×s | 417.57 | Joback Calculated Property |
η | 0.0002707 | Pa×s | 459.10 | Joback Calculated Property |
η | 0.0002074 | Pa×s | 500.64 | Joback Calculated Property |
ΔvapH | [43.09; 61.60] | kJ/mol | [368.50; 499.30] | ![]() |
ΔvapH | 61.60 | kJ/mol | 368.50 | NIST |
ΔvapH | 43.09 | kJ/mol | 499.30 | KDB |
ρl | [819.50; 889.10] | kg/m3 | [253.15; 343.15] | ![]() |
T(K) Liquid Density (kg/m3) 820 830 840 850 860 870 880 890 300 | ||||
ρl | 889.10 | kg/m3 | 253.15 | Density... |
ρl | 862.40 | kg/m3 | 288.15 | Density... |
ρl | 858.60 | kg/m3 | 293.15 | Density... |
ρl | 857.69 | kg/m3 | 293.15 | Density... |
ρl | 850.09 | kg/m3 | 303.15 | Density... |
ρl | 851.00 | kg/m3 | 303.15 | Density... |
ρl | 843.40 | kg/m3 | 313.15 | Density... |
ρl | 842.49 | kg/m3 | 313.15 | Density... |
ρl | 835.80 | kg/m3 | 323.15 | Density... |
ρl | 834.87 | kg/m3 | 323.15 | Density... |
ρl | 827.48 | kg/m3 | 333.15 | Density... |
ρl | 828.20 | kg/m3 | 333.15 | Density... |
ρl | 819.50 | kg/m3 | 343.15 | Density... |
γ | 0.03 | N/m | 294.40 | Densiti... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [367.43; 531.55] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47833e+01 | |||
Coefficient B | -4.48545e+03 | |||
Coefficient C | -5.79950e+01 | |||
Temperature range, min. | 367.43 | |||
Temperature range, max. | 531.55 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 367.43 | Calculated Property |
Pvap | 2.99 | kPa | 385.67 | Calculated Property |
Pvap | 6.15 | kPa | 403.90 | Calculated Property |
Pvap | 11.77 | kPa | 422.14 | Calculated Property |
Pvap | 21.18 | kPa | 440.37 | Calculated Property |
Pvap | 36.12 | kPa | 458.61 | Calculated Property |
Pvap | 58.81 | kPa | 476.84 | Calculated Property |
Pvap | 91.94 | kPa | 495.08 | Calculated Property |
Pvap | 138.67 | kPa | 513.31 | Calculated Property |
Pvap | 202.64 | kPa | 531.55 | Calculated Property |
Pvap | [5.66e-07; 2288.15] | kPa | [212.00; 698.00] |
KDB Vap...
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Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.17344e+01 | |||
Coefficient B | -1.01347e+04 | |||
Coefficient C | -1.09214e+01 | |||
Coefficient D | 4.18024e-06 | |||
Temperature range, min. | 212.00 | |||
Temperature range, max. | 698.00 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 400 600 | ||||
Pvap | 5.66e-07 | kPa | 212.00 | Calculated Property |
Pvap | 8.67e-04 | kPa | 266.00 | Calculated Property |
Pvap | 0.08 | kPa | 320.00 | Calculated Property |
Pvap | 1.68 | kPa | 374.00 | Calculated Property |
Pvap | 14.11 | kPa | 428.00 | Calculated Property |
Pvap | 67.17 | kPa | 482.00 | Calculated Property |
Pvap | 220.44 | kPa | 536.00 | Calculated Property |
Pvap | 562.30 | kPa | 590.00 | Calculated Property |
Pvap | 1205.29 | kPa | 644.00 | Calculated Property |
Pvap | 2288.15 | kPa | 698.00 | Calculated Property |
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