Property | Value | Unit | Source |
---|---|---|---|
PAff | 837.00 | kJ/mol | NIST |
BasG | 808.00 | kJ/mol | NIST |
ΔcH°liquid | [-3574.08; -3570.50] | kJ/mol |
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ΔcH°liquid | -3570.50 ± 3.00 | kJ/mol | NIST |
ΔcH°liquid | -3574.08 ± 0.48 | kJ/mol | NIST |
ΔfG° | 91.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [100.40; 109.00] | kJ/mol |
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ΔfH°gas | 100.40 ± 3.10 | kJ/mol | NIST |
ΔfH°gas | 109.00 | kJ/mol | NIST |
ΔfH°gas | 104.75 ± 0.59 | kJ/mol | NIST |
ΔfH°liquid | [66.10; 69.70] | kJ/mol |
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ΔfH°liquid | 66.10 ± 3.10 | kJ/mol | NIST |
ΔfH°liquid | 69.70 ± 0.58 | kJ/mol | NIST |
ΔfusH° | 4.50 | kJ/mol | Joback Calculated Property |
ΔvapH° | [34.30; 35.10] | kJ/mol |
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ΔvapH° | 34.30 | kJ/mol | NIST |
ΔvapH° | 34.30 | kJ/mol | NIST |
ΔvapH° | 35.05 ± 0.04 | kJ/mol | NIST |
ΔvapH° | 35.10 | kJ/mol | NIST |
IE | [8.65; 8.82] | eV |
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IE | 8.82 | eV | NIST |
IE | 8.82 ± 0.02 | eV | NIST |
IE | 8.82 ± 0.02 | eV | NIST |
IE | Outlier 8.65 ± 0.05 | eV | NIST |
IE | 8.80 | eV | NIST |
IE | 8.82 | eV | NIST |
IE | 8.82 | eV | NIST |
IE | 8.80 | eV | NIST |
IE | 8.82 | eV | NIST |
log10WS | [-2.06; -1.97] |
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|
log10WS | -1.97 | Aq. Sol... | |
log10WS | -2.06 | Estimat... | |
logPoct/wat | 1.893 | Crippen Calculated Property | |
McVol | 75.940 | ml/mol | McGowan Calculated Property |
Pc | 4540.80 | kPa | Joback Calculated Property |
Inp | [685.00; 738.00] |
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|
Inp | 725.30 | NIST | |
Inp | 724.90 | NIST | |
Inp | 709.20 | NIST | |
Inp | 718.00 | NIST | |
Inp | 706.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 690.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 698.00 | NIST | |
Inp | 687.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 700.00 | NIST | |
Inp | 700.00 | NIST | |
Inp | 685.00 | NIST | |
Inp | 690.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 698.00 | NIST | |
Inp | 694.00 | NIST | |
Inp | 707.00 | NIST | |
Inp | 696.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | Outlier 738.00 | NIST | |
Inp | 706.00 | NIST | |
Inp | 713.00 | NIST | |
Inp | 708.00 | NIST | |
Inp | 708.00 | NIST | |
Inp | 692.00 | NIST | |
Inp | Outlier 738.00 | NIST | |
I | [914.00; 939.00] |
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|
I | 932.00 | NIST | |
I | 939.00 | NIST | |
I | 939.00 | NIST | |
I | 914.00 | NIST | |
I | 939.00 | NIST | |
S°liquid | 189.37 | J/mol×K | NIST |
Tboil | [354.70; 362.70] | K |
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Tboil | 354.70 | K | NIST |
Tboil | 362.70 ± 0.20 | K | NIST |
Tboil | 362.55 ± 0.30 | K | NIST |
Tc | 568.24 | K | Joback Calculated Property |
Tfus | [222.83; 351.00] | K |
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Tfus | 224.05 | K | Aq. Sol... |
Tfus | 222.83 ± 0.20 | K | NIST |
Tfus | 351.00 ± 4.00 | K | NIST |
Ttriple | 224.00 ± 0.20 | K | NIST |
Vc | 0.278 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [112.28; 174.29] | J/mol×K | [359.22; 568.24] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 110 120 130 140 150 160 170 180 400 450 500 550 | ||||
Cp,gas | 112.28 | J/mol×K | 359.22 | Joback Calculated Property |
Cp,gas | 124.27 | J/mol×K | 394.06 | Joback Calculated Property |
Cp,gas | 135.57 | J/mol×K | 428.89 | Joback Calculated Property |
Cp,gas | 146.19 | J/mol×K | 463.73 | Joback Calculated Property |
Cp,gas | 156.16 | J/mol×K | 498.57 | Joback Calculated Property |
Cp,gas | 165.52 | J/mol×K | 533.40 | Joback Calculated Property |
Cp,gas | 174.29 | J/mol×K | 568.24 | Joback Calculated Property |
Cp,liquid | [142.20; 145.94] | J/mol×K | [298.15; 298.15] | ![]() |
Cp,liquid | 142.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 145.94 | J/mol×K | 298.15 | NIST |
η | [0.0002528; 0.0065358] | Pa×s | [170.52; 359.22] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 1.00e-3 2.00e-3 3.00e-3 4.00e-3 5.00e-3 6.00e-3 7.00e-3 200 250 300 350 | ||||
η | 0.0065358 | Pa×s | 170.52 | Joback Calculated Property |
η | 0.0024921 | Pa×s | 201.97 | Joback Calculated Property |
η | 0.0012321 | Pa×s | 233.42 | Joback Calculated Property |
η | 0.0007201 | Pa×s | 264.87 | Joback Calculated Property |
η | 0.0004717 | Pa×s | 296.32 | Joback Calculated Property |
η | 0.0003351 | Pa×s | 327.77 | Joback Calculated Property |
η | 0.0002528 | Pa×s | 359.22 | Joback Calculated Property |
ΔfusH | [0.82; 5.72] | kJ/mol | [192.00; 224.00] | ![]() |
ΔfusH | 0.82 | kJ/mol | 192.00 | NIST |
ΔfusH | 5.72 | kJ/mol | 224.00 | NIST |
ΔfusH | 5.72 | kJ/mol | 224.00 | NIST |
ΔvapH | [33.90; 34.00] | kJ/mol | [313.00; 332.00] | ![]() |
ΔvapH | 33.90 | kJ/mol | 313.00 | NIST |
ΔvapH | 34.00 | kJ/mol | 332.00 | NIST |
ΔfusS | [4.25; 25.51] | J/mol×K | [192.00; 224.00] | ![]() |
ΔfusS | 4.25 | J/mol×K | 192.00 | NIST |
ΔfusS | 25.51 | J/mol×K | 224.00 | NIST |
λ | [0.13; 0.16] | W/m×K | [258.46; 328.93] | ![]() |
T(K) Liquid thermal conductivity (W/m×K) 0.14 0.14 0.15 0.15 0.16 0.16 260 280 300 320 | ||||
λ | 0.16 | W/m×K | 258.46 | Thermal... |
λ | 0.16 | W/m×K | 258.67 | Thermal... |
λ | 0.16 | W/m×K | 258.82 | Thermal... |
λ | 0.16 | W/m×K | 264.86 | Thermal... |
λ | 0.16 | W/m×K | 265.08 | Thermal... |
λ | 0.16 | W/m×K | 265.23 | Thermal... |
λ | 0.15 | W/m×K | 279.38 | Thermal... |
λ | 0.15 | W/m×K | 279.60 | Thermal... |
λ | 0.15 | W/m×K | 279.76 | Thermal... |
λ | 0.15 | W/m×K | 296.20 | Thermal... |
λ | 0.15 | W/m×K | 296.43 | Thermal... |
λ | 0.15 | W/m×K | 296.60 | Thermal... |
λ | 0.14 | W/m×K | 313.90 | Thermal... |
λ | 0.14 | W/m×K | 314.13 | Thermal... |
λ | 0.14 | W/m×K | 314.31 | Thermal... |
λ | 0.13 | W/m×K | 328.51 | Thermal... |
λ | 0.13 | W/m×K | 328.75 | Thermal... |
λ | 0.13 | W/m×K | 328.93 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [276.86; 366.58] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.42725e+01 | |||
Coefficient B | -2.23809e+03 | |||
Coefficient C | -1.16823e+02 | |||
Temperature range, min. | 276.86 | |||
Temperature range, max. | 366.58 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 276.86 | Calculated Property |
Pvap | 3.03 | kPa | 286.83 | Calculated Property |
Pvap | 6.28 | kPa | 296.80 | Calculated Property |
Pvap | 12.06 | kPa | 306.77 | Calculated Property |
Pvap | 21.70 | kPa | 316.74 | Calculated Property |
Pvap | 36.93 | kPa | 326.70 | Calculated Property |
Pvap | 59.89 | kPa | 336.67 | Calculated Property |
Pvap | 93.14 | kPa | 346.64 | Calculated Property |
Pvap | 139.62 | kPa | 356.61 | Calculated Property |
Pvap | 202.65 | kPa | 366.58 | Calculated Property |
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