Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2850 | KDB | |
PAff | 799.40 | kJ/mol | NIST |
BasG | 768.40 | kJ/mol | NIST |
μ | 2.00 | debye | KDB |
η | 0.0004000 | Pa×s | Densiti... |
ΔfG° | -230.14 | kJ/mol | Joback Calculated Property |
ΔfH°gas | [-398.00; -361.70] | kJ/mol | |
ΔfH°gas | -371.50 | kJ/mol | KDB |
ΔfH°gas | -361.70 | kJ/mol | NIST |
ΔfH°gas | -398.00 | kJ/mol | NIST |
ΔfH°liquid | [-430.50; -394.20] | kJ/mol | |
ΔfH°liquid | -394.20 ± 0.80 | kJ/mol | NIST |
ΔfH°liquid | -430.50 | kJ/mol | NIST |
ΔfusH° | 7.00 | kJ/mol | Joback Calculated Property |
ΔvapH° | [30.10; 32.50] | kJ/mol | |
ΔvapH° | 32.11 | kJ/mol | NIST |
ΔvapH° | 32.20 | kJ/mol | NIST |
ΔvapH° | 32.50 | kJ/mol | NIST |
ΔvapH° | 30.10 ± 0.01 | kJ/mol | NIST |
IE | [10.61; 10.62] | eV | |
IE | 10.61 ± 0.01 | eV | NIST |
IE | 10.61 ± 0.05 | eV | NIST |
IE | 10.61 ± 0.05 | eV | NIST |
IE | Outlier 10.62 | eV | NIST |
IE | 10.61 ± 0.01 | eV | NIST |
IE | 10.61 | eV | NIST |
log10WS | [0.15; 0.15] | ||
log10WS | 0.15 | Aq. Sol... | |
log10WS | 0.15 | Estimat... | |
logPoct/wat | 0.179 | Crippen Calculated Property | |
McVol | 60.570 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
Pc | [4737.00; 4981.00] | kPa | |
Pc | 4740.00 | kPa | KDB |
Pc | 4738.00 ± 101.32 | kPa | NIST |
Pc | 4737.00 ± 40.00 | kPa | NIST |
Pc | 4981.00 ± 202.65 | kPa | NIST |
Pc | 4930.00 ± 202.65 | kPa | NIST |
ρc | [314.83; 323.20] | kg/m3 | |
ρc | 323.20 ± 5.19 | kg/m3 | NIST |
ρc | 323.20 ± 3.70 | kg/m3 | NIST |
ρc | 314.83 ± 5.93 | kg/m3 | NIST |
Inp | [455.00; 545.00] | ||
Inp | 457.00 | NIST | |
Inp | 501.00 | NIST | |
Inp | 463.00 | NIST | |
Inp | 474.00 | NIST | |
Inp | 465.00 | NIST | |
Inp | 469.00 | NIST | |
Inp | 468.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 456.00 | NIST | |
Inp | 487.00 | NIST | |
Inp | 455.00 | NIST | |
Inp | 468.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 481.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 481.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 504.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 478.00 | NIST | |
Inp | 500.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 510.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 530.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 487.00 | NIST | |
Inp | 521.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 521.00 | NIST | |
Inp | Outlier 545.00 | NIST | |
Inp | 502.00 | NIST | |
Inp | 501.00 | NIST | |
Inp | 495.00 | NIST | |
Inp | 487.00 | NIST | |
Inp | Outlier 545.00 | NIST | |
Inp | 481.00 | NIST | |
Inp | 502.00 | NIST | |
I | [800.00; 849.10] | ||
I | 842.00 | NIST | |
I | 820.00 | NIST | |
I | 847.00 | NIST | |
I | 832.00 | NIST | |
I | 825.00 | NIST | |
I | 825.00 | NIST | |
I | 848.00 | NIST | |
I | 837.00 | NIST | |
I | 822.00 | NIST | |
I | 849.10 | NIST | |
I | 820.00 | NIST | |
I | 814.00 | NIST | |
I | 811.00 | NIST | |
I | 821.00 | NIST | |
I | 834.00 | NIST | |
I | 820.00 | NIST | |
I | 800.00 | NIST | |
I | 825.00 | NIST | |
I | 806.00 | NIST | |
I | 804.00 | NIST | |
I | 830.00 | NIST | |
I | 806.00 | NIST | |
I | 810.00 | NIST | |
I | 822.00 | NIST | |
I | 823.00 | NIST | |
I | 849.10 | NIST | |
Tboil | [325.85; 328.15] | K | |
Tboil | 327.50 | K | KDB |
Tboil | 327.33 | K | Solutio... |
Tboil | 327.29 | K | Isobari... |
Tboil | 327.33 | K | Isobari... |
Tboil | 327.32 | K | Isobari... |
Tboil | 327.45 ± 0.40 | K | NIST |
Tboil | Outlier 326.20 | K | NIST |
Tboil | 327.70 | K | NIST |
Tboil | 327.50 | K | NIST |
Tboil | 327.15 ± 0.30 | K | NIST |
Tboil | 327.35 ± 0.20 | K | NIST |
Tboil | 327.65 ± 2.00 | K | NIST |
Tboil | 327.45 ± 1.00 | K | NIST |
Tboil | 327.45 ± 2.00 | K | NIST |
Tboil | 327.30 ± 0.40 | K | NIST |
Tboil | 327.30 ± 0.50 | K | NIST |
Tboil | 327.15 ± 2.00 | K | NIST |
Tboil | Outlier 326.35 ± 1.00 | K | NIST |
Tboil | 327.30 ± 0.20 | K | NIST |
Tboil | 327.40 ± 0.60 | K | NIST |
Tboil | 327.00 ± 2.00 | K | NIST |
Tboil | Outlier 325.85 ± 2.00 | K | NIST |
Tboil | 327.30 ± 0.50 | K | NIST |
Tboil | 327.30 ± 0.50 | K | NIST |
Tboil | 327.30 ± 0.50 | K | NIST |
Tboil | 326.55 ± 1.00 | K | NIST |
Tboil | 327.45 ± 2.00 | K | NIST |
Tboil | 327.20 ± 0.30 | K | NIST |
Tboil | 327.45 ± 0.50 | K | NIST |
Tboil | 327.50 ± 0.50 | K | NIST |
Tboil | 326.65 ± 2.00 | K | NIST |
Tboil | 327.47 ± 0.50 | K | NIST |
Tboil | 327.10 ± 2.00 | K | NIST |
Tboil | 328.00 ± 2.00 | K | NIST |
Tboil | 327.35 ± 2.00 | K | NIST |
Tboil | 328.15 ± 2.00 | K | NIST |
Tboil | 328.05 ± 2.00 | K | NIST |
Tboil | 328.05 ± 2.00 | K | NIST |
Tc | [503.20; 511.80] | K | |
Tc | 508.50 | K | KDB |
Tc | 508.40 | K | NIST |
Tc | 508.50 ± 1.00 | K | NIST |
Tc | 508.50 ± 1.00 | K | NIST |
Tc | 506.30 ± 2.00 | K | NIST |
Tc | 511.80 ± 2.00 | K | NIST |
Tc | 503.20 ± 4.00 | K | NIST |
Tfus | [192.65; 193.75] | K | |
Tfus | 192.75 | K | Aq. Sol... |
Tfus | 193.50 | K | KDB |
Tfus | 193.55 ± 0.50 | K | NIST |
Tfus | 193.00 ± 2.00 | K | NIST |
Tfus | 193.75 ± 0.40 | K | NIST |
Tfus | 192.65 ± 0.30 | K | NIST |
Vc | 0.229 | m3/kmol | KDB |
Zc | 0.2567360 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [101.20; 129.73] | J/mol×K | [339.12; 513.09] | |
T(K) Ideal gas heat capacity (J/mol×K) 100 105 110 115 120 125 130 350 400 450 500 | ||||
Cp,gas | 101.20 | J/mol×K | 339.12 | Joback Calculated Property |
Cp,gas | 106.21 | J/mol×K | 368.11 | Joback Calculated Property |
Cp,gas | 111.13 | J/mol×K | 397.11 | Joback Calculated Property |
Cp,gas | 115.94 | J/mol×K | 426.10 | Joback Calculated Property |
Cp,gas | 120.65 | J/mol×K | 455.10 | Joback Calculated Property |
Cp,gas | 125.25 | J/mol×K | 484.09 | Joback Calculated Property |
Cp,gas | 129.73 | J/mol×K | 513.09 | Joback Calculated Property |
Cp,liquid | [144.30; 158.20] | J/mol×K | [290.00; 298.15] | |
Cp,liquid | 158.20 | J/mol×K | 290.00 | NIST |
Cp,liquid | 148.10 | J/mol×K | 294.70 | NIST |
Cp,liquid | 148.10 | J/mol×K | 294.70 | NIST |
Cp,liquid | 144.30 | J/mol×K | 298.15 | NIST |
η | [0.0003000; 0.0004020] | Pa×s | [293.15; 323.15] | |
T(K) Dynamic viscosity (Pa×s) 3.00e-4 3.20e-4 3.40e-4 3.60e-4 3.80e-4 4.00e-4 300 310 320 | ||||
η | 0.0004020 | Pa×s | 293.15 | Density... |
η | 0.0003810 | Pa×s | 298.15 | Density... |
η | 0.0003660 | Pa×s | 303.15 | Viscosi... |
η | 0.0003620 | Pa×s | 303.15 | Density... |
η | 0.0003730 | Pa×s | 303.15 | Physica... |
η | 0.0003450 | Pa×s | 308.15 | Density... |
η | 0.0003450 | Pa×s | 308.15 | Physica... |
η | 0.0003390 | Pa×s | 313.15 | Viscosi... |
η | 0.0003290 | Pa×s | 313.15 | Density... |
η | 0.0003240 | Pa×s | 313.15 | Physica... |
η | 0.0003140 | Pa×s | 318.15 | Density... |
η | 0.0003000 | Pa×s | 323.15 | Density... |
ΔvapH | [29.80; 35.80] | kJ/mol | [274.50; 412.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 35 36 300 350 400 | ||||
ΔvapH | 35.80 | kJ/mol | 274.50 | NIST |
ΔvapH | 31.60 ± 0.10 | kJ/mol | 304.00 | NIST |
ΔvapH | 31.40 | kJ/mol | 313.00 | NIST |
ΔvapH | 30.90 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 29.91 | kJ/mol | 327.50 | NIST |
ΔvapH | 29.80 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 29.90 | kJ/mol | 412.50 | NIST |
Pvap | 101.32 | kPa | 327.33 | Isobari... |
n0 | [1.35520; 1.35800] | [298.15; 303.15] | ||
n0 | 1.35800 | 298.15 | Thermod... | |
n0 | 1.35520 | 303.15 | Excess ... | |
ρl | [876.00; 927.00] | kg/m3 | [289.00; 323.15] | |
T(K) Liquid Density (kg/m3) 880 890 900 910 920 930 290 300 310 320 | ||||
ρl | 927.00 | kg/m3 | 289.00 | KDB |
ρl | 923.40 | kg/m3 | 291.15 | Experim... |
ρl | 916.60 | kg/m3 | 293.15 | Densiti... |
ρl | 914.35 | kg/m3 | 298.15 | Experim... |
ρl | 910.10 | kg/m3 | 298.15 | Densiti... |
ρl | 903.60 | kg/m3 | 303.15 | Densiti... |
ρl | 897.10 | kg/m3 | 308.15 | Densiti... |
ρl | 890.50 | kg/m3 | 313.15 | Densiti... |
ρl | 883.00 | kg/m3 | 318.15 | Densiti... |
ρl | 876.00 | kg/m3 | 323.15 | Densiti... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 4887.31] | kPa | [240.08; 508.40] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.46571e+01 | |||
Coefficient B | -2.89533e+03 | |||
Coefficient C | -3.85850e+01 | |||
Temperature range, min. | 240.08 | |||
Temperature range, max. | 508.40 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
Pvap | 1.33 | kPa | 240.08 | Calculated Property |
Pvap | 8.50 | kPa | 269.89 | Calculated Property |
Pvap | 35.48 | kPa | 299.71 | Calculated Property |
Pvap | 110.53 | kPa | 329.52 | Calculated Property |
Pvap | 278.75 | kPa | 359.33 | Calculated Property |
Pvap | 600.63 | kPa | 389.15 | Calculated Property |
Pvap | 1147.48 | kPa | 418.96 | Calculated Property |
Pvap | 1995.33 | kPa | 448.77 | Calculated Property |
Pvap | 3219.01 | kPa | 478.59 | Calculated Property |
Pvap | 4887.31 | kPa | 508.40 | Calculated Property |
Pvap | [0.02; 4690.28] | kPa | [193.55; 508.40] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.34086e+01 | |||
Coefficient B | -5.70647e+03 | |||
Coefficient C | -7.24275e+00 | |||
Coefficient D | 5.41841e-06 | |||
Temperature range, min. | 193.55 | |||
Temperature range, max. | 508.40 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 200 300 400 500 | ||||
Pvap | 0.02 | kPa | 193.55 | Calculated Property |
Pvap | 0.54 | kPa | 228.53 | Calculated Property |
Pvap | 5.80 | kPa | 263.52 | Calculated Property |
Pvap | 33.10 | kPa | 298.50 | Calculated Property |
Pvap | 124.22 | kPa | 333.48 | Calculated Property |
Pvap | 349.77 | kPa | 368.47 | Calculated Property |
Pvap | 803.96 | kPa | 403.45 | Calculated Property |
Pvap | 1596.30 | kPa | 438.43 | Calculated Property |
Pvap | 2847.13 | kPa | 473.42 | Calculated Property |
Pvap | 4690.28 | kPa | 508.40 | Calculated Property |
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