Property | Value | Unit | Source |
---|---|---|---|
PAff | 946.60 | kJ/mol | NIST |
BasG | 892.40 | kJ/mol | NIST |
ΔfG° | -403.52 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -737.33 | kJ/mol | Joback Calculated Property |
ΔfusH° | 21.23 | kJ/mol | Joback Calculated Property |
ΔvapH° | 63.70 ± 3.30 | kJ/mol | NIST |
IE | 9.80 | eV | NIST |
log10WS | 0.48 | Crippen Calculated Property | |
logPoct/wat | 0.312 | Crippen Calculated Property | |
McVol | 147.060 | ml/mol | McGowan Calculated Property |
Pc | 2370.28 | kPa | Joback Calculated Property |
Inp | [205.88; 1232.30] |
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|
Inp | 1232.00 | NIST | |
Inp | 1232.30 | NIST | |
Inp | 205.88 | NIST | |
Inp | 208.42 | NIST | |
Inp | 205.88 | NIST | |
Inp | 1232.30 | NIST | |
Inp | 1232.00 | NIST | |
S°liquid | 492.90 | J/mol×K | NIST |
Tboil | [489.00; 489.20] | K |
![]() |
Tboil | 489.20 | K | NIST |
Tboil | 489.00 ± 2.00 | K | NIST |
Tboil | 489.15 | K | NIST |
Tboil | 489.00 | K | NIST |
Tc | 636.37 | K | Joback Calculated Property |
Tfus | [228.00; 228.15] | K |
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Tfus | 228.15 | K | NIST |
Tfus | 228.00 | K | NIST |
Ttriple | 229.30 ± 0.20 | K | NIST |
Vc | 0.555 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [331.93; 401.19] | J/mol×K | [472.12; 636.37] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 330 340 350 360 370 380 390 400 500 550 600 | ||||
Cp,gas | 331.93 | J/mol×K | 472.12 | Joback Calculated Property |
Cp,gas | 344.16 | J/mol×K | 499.50 | Joback Calculated Property |
Cp,gas | 356.14 | J/mol×K | 526.87 | Joback Calculated Property |
Cp,gas | 367.85 | J/mol×K | 554.25 | Joback Calculated Property |
Cp,gas | 379.27 | J/mol×K | 581.62 | Joback Calculated Property |
Cp,gas | 390.39 | J/mol×K | 609.00 | Joback Calculated Property |
Cp,gas | 401.19 | J/mol×K | 636.37 | Joback Calculated Property |
Cp,liquid | [359.00; 382.00] | J/mol×K | [298.15; 353.15] | ![]() |
T(K) Liquid phase heat capacity (J/mol×K) 360 365 370 375 380 300 320 340 | ||||
Cp,liquid | 368.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 367.78 | J/mol×K | 298.15 | NIST |
Cp,liquid | 359.00 | J/mol×K | 303.15 | Molar H... |
Cp,liquid | 364.00 | J/mol×K | 308.15 | Molar H... |
Cp,liquid | 366.00 | J/mol×K | 313.15 | Molar H... |
Cp,liquid | 368.00 | J/mol×K | 318.15 | Molar H... |
Cp,liquid | 370.00 | J/mol×K | 323.15 | Molar H... |
Cp,liquid | 371.00 | J/mol×K | 328.15 | Molar H... |
Cp,liquid | 373.00 | J/mol×K | 333.15 | Molar H... |
Cp,liquid | 375.00 | J/mol×K | 338.15 | Molar H... |
Cp,liquid | 379.00 | J/mol×K | 343.15 | Molar H... |
Cp,liquid | 381.00 | J/mol×K | 348.15 | Molar H... |
Cp,liquid | 382.00 | J/mol×K | 353.15 | Molar H... |
η | [0.0007260; 0.0035600] | Pa×s | [273.15; 363.15] | ![]() |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 300 350 | ||||
η | 0.0035600 | Pa×s | 273.15 | Density... |
η | 0.0031000 | Pa×s | 278.15 | Density... |
η | 0.0027500 | Pa×s | 283.15 | Density... |
η | 0.0024500 | Pa×s | 288.15 | Density... |
η | 0.0021900 | Pa×s | 293.15 | Density... |
η | 0.0019600 | Pa×s | 298.15 | Density... |
η | 0.0017800 | Pa×s | 303.15 | Density... |
η | 0.0017700 | Pa×s | 303.15 | Densiti... |
η | 0.0014800 | Pa×s | 313.15 | Densiti... |
η | 0.0014800 | Pa×s | 313.15 | Density... |
η | 0.0012500 | Pa×s | 323.15 | Density... |
η | 0.0012600 | Pa×s | 323.15 | Densiti... |
η | 0.0010800 | Pa×s | 333.15 | Density... |
η | 0.0010800 | Pa×s | 333.15 | Densiti... |
η | 0.0009360 | Pa×s | 343.15 | Density... |
η | 0.0009450 | Pa×s | 343.15 | Densiti... |
η | 0.0008210 | Pa×s | 353.15 | Density... |
η | 0.0007260 | Pa×s | 363.15 | Density... |
ΔfusH | [23.71; 23.71] | kJ/mol | [229.30; 229.30] | ![]() |
ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
ΔfusH | 23.71 | kJ/mol | 229.30 | NIST |
n0 | [1.41250; 1.42500] | [288.15; 318.15] | ![]() |
|
n0 | 1.42500 | 288.15 | Liquid ... | |
n0 | 1.42090 | 298.15 | Liquid ... | |
n0 | 1.41670 | 308.15 | Liquid ... | |
n0 | 1.41250 | 318.15 | Liquid ... | |
ρl | [909.70; 994.10] | kg/m3 | [283.15; 373.15] | ![]() |
T(K) Liquid Density (kg/m3) 920 940 960 980 1000 300 320 340 360 | ||||
ρl | 994.10 | kg/m3 | 283.15 | Thermop... |
ρl | 990.80 | kg/m3 | 288.15 | Thermop... |
ρl | 989.40 | kg/m3 | 288.15 | Thermop... |
ρl | 984.60 | kg/m3 | 293.15 | Thermop... |
ρl | 986.00 | kg/m3 | 293.15 | Thermop... |
ρl | 981.50 | kg/m3 | 298.15 | Thermop... |
ρl | 980.62 | kg/m3 | 298.15 | Thermod... |
ρl | 979.90 | kg/m3 | 298.15 | Thermop... |
ρl | 980.42 | kg/m3 | 298.15 | Liquid-... |
ρl | 976.70 | kg/m3 | 303.15 | Thermop... |
ρl | 975.10 | kg/m3 | 303.15 | Thermop... |
ρl | 971.90 | kg/m3 | 308.15 | Thermop... |
ρl | 970.40 | kg/m3 | 308.15 | Thermop... |
ρl | 967.20 | kg/m3 | 313.15 | Thermop... |
ρl | 965.60 | kg/m3 | 313.15 | Thermop... |
ρl | 962.40 | kg/m3 | 318.15 | Thermop... |
ρl | 956.10 | kg/m3 | 323.15 | Thermop... |
ρl | 957.70 | kg/m3 | 323.15 | Thermop... |
ρl | 952.90 | kg/m3 | 328.15 | Thermop... |
ρl | 946.50 | kg/m3 | 333.15 | Thermop... |
ρl | 948.10 | kg/m3 | 333.15 | Thermop... |
ρl | 943.30 | kg/m3 | 338.15 | Thermop... |
ρl | 936.90 | kg/m3 | 343.15 | Thermop... |
ρl | 938.60 | kg/m3 | 343.15 | Thermop... |
ρl | 933.80 | kg/m3 | 348.15 | Thermop... |
ρl | 929.00 | kg/m3 | 353.15 | Thermop... |
ρl | 924.20 | kg/m3 | 358.15 | Thermop... |
ρl | 919.40 | kg/m3 | 363.15 | Thermop... |
ρl | 914.50 | kg/m3 | 368.15 | Thermop... |
ρl | 909.70 | kg/m3 | 373.15 | Thermop... |
ΔfusS | 103.40 | J/mol×K | 229.30 | NIST |
γ | [0.03; 0.03] | N/m | [298.15; 318.15] | ![]() |
γ | 0.03 | N/m | 298.15 | Volumet... |
γ | 0.03 | N/m | 308.15 | Volumet... |
γ | 0.03 | N/m | 318.15 | Volumet... |
λ | [0.12; 0.14] | W/m×K | [302.75; 392.16] | ![]() |
λ | 0.14 | W/m×K | 302.75 | Thermal... |
λ | 0.14 | W/m×K | 332.54 | Thermal... |
λ | 0.13 | W/m×K | 362.39 | Thermal... |
λ | 0.12 | W/m×K | 392.16 | Thermal... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [376.60; 376.70] | K | [1.30; 1.30] |
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Tboilr | 376.70 | K | 1.30 | NIST |
Tboilr | 376.60 | K | 1.30 | NIST |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
293.15 | 100.00 | 0.0021 |
293.15 | 20000.00 | 0.0025 |
293.15 | 40000.00 | 0.0030 |
293.15 | 60000.00 | 0.0034 |
293.15 | 80000.00 | 0.0039 |
293.15 | 100000.00 | 0.0044 |
313.15 | 100.00 | 0.0015 |
313.15 | 20000.00 | 0.0018 |
313.15 | 40000.00 | 0.0020 |
313.15 | 60000.00 | 0.0024 |
313.15 | 80000.00 | 0.0027 |
313.15 | 100000.00 | 0.0030 |
333.15 | 100.00 | 0.0011 |
333.15 | 20000.00 | 0.0013 |
333.15 | 40000.00 | 0.0015 |
333.15 | 60000.00 | 0.0017 |
333.15 | 80000.00 | 0.0019 |
333.15 | 100000.00 | 0.0021 |
353.15 | 100.00 | 0.0008 |
353.15 | 20000.00 | 0.0010 |
353.15 | 40000.00 | 0.0011 |
353.15 | 60000.00 | 0.0013 |
353.15 | 80000.00 | 0.0015 |
353.15 | 100000.00 | 0.0016 |
Reference |
Fixed | Measured | |
---|---|---|
Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
293.15 | 100.00 | 1361.9 |
293.15 | 10000.00 | 1403.1 |
293.15 | 20000.00 | 1442.5 |
293.15 | 30000.00 | 1479.3 |
293.15 | 40000.00 | 1514.7 |
293.15 | 50000.00 | 1547.8 |
293.15 | 60000.00 | 1579.5 |
293.15 | 70000.00 | 1610.0 |
293.15 | 80000.00 | 1639.3 |
293.15 | 90000.00 | 1667.4 |
293.15 | 100000.00 | 1694.6 |
303.15 | 100.00 | 1323.2 |
303.15 | 10000.00 | 1366.5 |
303.15 | 20000.00 | 1407.2 |
303.15 | 30000.00 | 1445.2 |
303.15 | 40000.00 | 1481.6 |
303.15 | 50000.00 | 1515.7 |
303.15 | 60000.00 | 1548.2 |
303.15 | 70000.00 | 1579.4 |
303.15 | 80000.00 | 1609.3 |
303.15 | 90000.00 | 1638.2 |
303.15 | 100000.00 | 1665.9 |
313.15 | 100.00 | 1285.1 |
313.15 | 10000.00 | 1330.0 |
313.15 | 20000.00 | 1372.2 |
313.15 | 30000.00 | 1411.8 |
313.15 | 40000.00 | 1448.8 |
313.15 | 50000.00 | 1484.1 |
313.15 | 60000.00 | 1517.5 |
313.15 | 70000.00 | 1549.7 |
313.15 | 80000.00 | 1580.3 |
313.15 | 90000.00 | 1609.9 |
313.15 | 100000.00 | 1638.1 |
323.15 | 100.00 | 1247.7 |
323.15 | 10000.00 | 1294.6 |
323.15 | 20000.00 | 1338.5 |
323.15 | 30000.00 | 1379.1 |
323.15 | 40000.00 | 1417.3 |
323.15 | 50000.00 | 1453.6 |
323.15 | 60000.00 | 1487.9 |
323.15 | 70000.00 | 1520.7 |
323.15 | 80000.00 | 1552.0 |
323.15 | 90000.00 | 1581.9 |
323.15 | 100000.00 | 1610.8 |
333.15 | 100.00 | 1210.9 |
333.15 | 10000.00 | 1259.5 |
333.15 | 20000.00 | 1304.8 |
333.15 | 30000.00 | 1346.9 |
333.15 | 40000.00 | 1386.3 |
333.15 | 50000.00 | 1423.4 |
333.15 | 60000.00 | 1458.8 |
333.15 | 70000.00 | 1492.1 |
333.15 | 80000.00 | 1524.3 |
333.15 | 90000.00 | 1554.8 |
333.15 | 100000.00 | 1584.3 |
343.15 | 100.00 | 1174.6 |
343.15 | 10000.00 | 1225.1 |
343.15 | 20000.00 | 1272.0 |
343.15 | 30000.00 | 1315.6 |
343.15 | 40000.00 | 1356.2 |
343.15 | 50000.00 | 1394.1 |
343.15 | 60000.00 | 1430.3 |
343.15 | 70000.00 | 1464.6 |
343.15 | 80000.00 | 1497.2 |
343.15 | 90000.00 | 1528.4 |
343.15 | 100000.00 | 1558.5 |
353.15 | 100.00 | 1138.7 |
353.15 | 10000.00 | 1191.5 |
353.15 | 20000.00 | 1240.0 |
353.15 | 30000.00 | 1284.6 |
353.15 | 40000.00 | 1326.2 |
353.15 | 50000.00 | 1365.6 |
353.15 | 60000.00 | 1402.4 |
353.15 | 70000.00 | 1437.6 |
353.15 | 80000.00 | 1470.9 |
353.15 | 90000.00 | 1502.6 |
353.15 | 100000.00 | 1533.4 |
Reference |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [372.99; 516.68] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.57644e+01 | |||
Coefficient B | -4.62697e+03 | |||
Coefficient C | -7.40300e+01 | |||
Temperature range, min. | 372.99 | |||
Temperature range, max. | 516.68 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 372.99 | Calculated Property |
Pvap | 2.92 | kPa | 388.96 | Calculated Property |
Pvap | 5.94 | kPa | 404.92 | Calculated Property |
Pvap | 11.30 | kPa | 420.89 | Calculated Property |
Pvap | 20.32 | kPa | 436.85 | Calculated Property |
Pvap | 34.79 | kPa | 452.82 | Calculated Property |
Pvap | 57.01 | kPa | 468.78 | Calculated Property |
Pvap | 89.92 | kPa | 484.75 | Calculated Property |
Pvap | 137.06 | kPa | 500.71 | Calculated Property |
Pvap | 202.66 | kPa | 516.68 | Calculated Property |
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