Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3620 | KDB | |
PAff | 811.50 | kJ/mol | NIST |
BasG | 780.90 | kJ/mol | NIST |
ΔcH°liquid | [-3632.30; -3632.30] | kJ/mol | |
ΔcH°liquid | -3632.30 ± 1.50 | kJ/mol | NIST |
ΔcH°liquid | -3632.30 | kJ/mol | NIST |
Cp,liquid | 166.41 | J/mol×K | Thermod... |
μ | 3.50 | debye | KDB |
EA | [0.26; 0.26] | eV | |
EA | 0.26 ± 0.10 | eV | NIST |
EA | 0.26 ± 0.02 | eV | NIST |
Tflash,oc | 348.15 | K | KDB |
ΔfG° | 261.00 | kJ/mol | KDB |
ΔfH°gas | [219.00; 219.00] | kJ/mol | |
ΔfH°gas | 219.00 | kJ/mol | KDB |
ΔfH°gas | 219.00 | kJ/mol | NIST |
ΔfH°gas | 219.00 | kJ/mol | NIST |
ΔfH°liquid | [163.20; 163.20] | kJ/mol | |
ΔfH°liquid | 163.20 ± 1.50 | kJ/mol | NIST |
ΔfH°liquid | 163.20 ± 1.50 | kJ/mol | NIST |
ΔfusH° | 9.43 | kJ/mol | Joback Calculated Property |
ΔvapH° | [55.48; 55.80] | kJ/mol | |
ΔvapH° | 55.48 | kJ/mol | NIST |
ΔvapH° | 55.80 | kJ/mol | NIST |
IE | [9.60; 10.13] | eV | |
IE | 9.73 ± 0.01 | eV | NIST |
IE | 9.73 ± 0.00 | eV | NIST |
IE | 9.60 | eV | NIST |
IE | Outlier 10.13 ± 0.03 | eV | NIST |
IE | 9.69 | eV | NIST |
IE | 9.62 | eV | NIST |
IE | 9.70 | eV | NIST |
IE | 9.77 | eV | NIST |
IE | 9.71 ± 0.01 | eV | NIST |
IE | 9.79 | eV | NIST |
IE | 9.80 | eV | NIST |
IE | 9.71 | eV | NIST |
IE | 9.71 | eV | NIST |
IE | 9.70 | eV | NIST |
IE | 9.72 | eV | NIST |
IE | 9.70 | eV | NIST |
IE | Outlier 10.02 | eV | NIST |
log10WS | [-1.00; -1.00] | ||
log10WS | -1.00 | Aq. Sol... | |
log10WS | -1.00 | Estimat... | |
logPoct/wat | 1.558 | Crippen Calculated Property | |
McVol | 87.110 | ml/mol | McGowan Calculated Property |
NFPA Fire | 1 | KDB | |
NFPA Health | 1 | KDB | |
NFPA Safety | 1 | KDB | |
Pc | [4210.00; 4220.00] | kPa | |
Pc | 4210.00 | kPa | KDB |
Pc | 4215.00 ± 4.00 | kPa | NIST |
Pc | 4220.00 ± 101.32 | kPa | NIST |
Pc | 4215.12 ± 151.99 | kPa | NIST |
Pc | 4215.12 ± 151.99 | kPa | NIST |
ρc | 313.18 ± 3.09 | kg/m3 | NIST |
Inp | [150.10; 1003.00] | ||
Inp | 953.00 | NIST | |
Inp | 936.00 | NIST | |
Inp | 965.00 | NIST | |
Inp | 973.00 | NIST | |
Inp | 994.00 | NIST | |
Inp | 937.30 | NIST | |
Inp | 987.90 | NIST | |
Inp | 986.00 | NIST | |
Inp | 940.10 | NIST | |
Inp | 983.40 | NIST | |
Inp | 976.00 | NIST | |
Inp | 983.00 | NIST | |
Inp | 1003.00 | NIST | |
Inp | 981.00 | NIST | |
Inp | 956.00 | NIST | |
Inp | 947.00 | NIST | |
Inp | 951.00 | NIST | |
Inp | 954.00 | NIST | |
Inp | 962.00 | NIST | |
Inp | 970.00 | NIST | |
Inp | 948.00 | NIST | |
Inp | 989.00 | NIST | |
Inp | 989.90 | NIST | |
Inp | 985.00 | NIST | |
Inp | 982.00 | NIST | |
Inp | 993.00 | NIST | |
Inp | 994.00 | NIST | |
Inp | 984.00 | NIST | |
Inp | 984.00 | NIST | |
Inp | 965.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 951.00 | NIST | |
Inp | 981.00 | NIST | |
Inp | 965.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 943.00 | NIST | |
Inp | 965.00 | NIST | |
Inp | 943.00 | NIST | |
Inp | 958.00 | NIST | |
Inp | 987.00 | NIST | |
Inp | 965.00 | NIST | |
Inp | 955.00 | NIST | |
Inp | Outlier 150.10 | NIST | |
Inp | Outlier 150.40 | NIST | |
Inp | 1003.00 | NIST | |
Inp | 953.00 | NIST | |
Inp | 993.00 | NIST | |
Inp | 988.00 | NIST | |
Inp | 992.00 | NIST | |
Inp | 987.00 | NIST | |
I | [1570.00; 1629.00] | ||
I | 1583.00 | NIST | |
I | Outlier 1629.00 | NIST | |
I | 1591.00 | NIST | |
I | 1570.00 | NIST | |
I | 1614.00 | NIST | |
I | 1583.00 | NIST | |
I | 1583.00 | NIST | |
I | 1583.00 | NIST | |
S°liquid | [209.10; 209.10] | J/mol×K | |
S°liquid | 209.10 | J/mol×K | NIST |
S°liquid | 209.10 | J/mol×K | NIST |
S°liquid | 209.10 | J/mol×K | NIST |
Tboil | [461.90; 464.50] | K | |
Tboil | 464.30 | K | KDB |
Tboil | 462.70 | K | NIST |
Tboil | 463.90 | K | NIST |
Tboil | 464.00 | K | NIST |
Tboil | 463.80 | K | NIST |
Tboil | 464.15 ± 0.30 | K | NIST |
Tboil | 463.85 ± 0.60 | K | NIST |
Tboil | Outlier 461.90 ± 1.00 | K | NIST |
Tboil | 464.10 ± 0.60 | K | NIST |
Tboil | 464.00 ± 0.40 | K | NIST |
Tboil | 464.30 ± 0.70 | K | NIST |
Tboil | 464.25 ± 0.30 | K | NIST |
Tboil | 464.50 ± 0.30 | K | NIST |
Tboil | 464.45 ± 0.30 | K | NIST |
Tboil | 463.85 ± 0.50 | K | NIST |
Tc | [699.20; 705.25] | K | |
Tc | 699.40 | K | KDB |
Tc | 699.40 ± 1.00 | K | NIST |
Tc | 699.20 ± 3.00 | K | NIST |
Tc | 701.25 ± 2.50 | K | NIST |
Tc | 699.35 ± 2.50 | K | NIST |
Tc | 700.45 ± 2.50 | K | NIST |
Tc | Outlier 705.25 ± 2.50 | K | NIST |
Tfus | [259.15; 286.15] | K | |
Tfus | 260.22 | K | Aq. Sol... |
Tfus | 260.40 | K | KDB |
Tfus | 260.00 | K | NIST |
Tfus | Outlier 286.15 ± 1.00 | K | NIST |
Tfus | 259.15 ± 0.00 | K | NIST |
Tfus | 260.28 ± 0.25 | K | NIST |
Tfus | 260.40 ± 0.15 | K | NIST |
Tfus | 259.35 ± 0.50 | K | NIST |
Tfus | 259.35 ± 0.40 | K | NIST |
Tfus | 260.05 ± 0.30 | K | NIST |
Ttriple | [260.33; 260.33] | K | |
Ttriple | 260.33 ± 0.02 | K | NIST |
Ttriple | 260.33 ± 0.02 | K | NIST |
Ttriple | 260.33 ± 0.02 | K | NIST |
Vc | 0.345 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [161.30; 206.96] | J/mol×K | [488.32; 724.27] | |
T(K) Ideal gas heat capacity (J/mol×K) 160 170 180 190 200 210 500 600 700 | ||||
Cp,gas | 161.30 | J/mol×K | 488.32 | Joback Calculated Property |
Cp,gas | 170.44 | J/mol×K | 527.64 | Joback Calculated Property |
Cp,gas | 178.93 | J/mol×K | 566.97 | Joback Calculated Property |
Cp,gas | 186.79 | J/mol×K | 606.29 | Joback Calculated Property |
Cp,gas | 194.06 | J/mol×K | 645.62 | Joback Calculated Property |
Cp,gas | 200.77 | J/mol×K | 684.94 | Joback Calculated Property |
Cp,gas | 206.96 | J/mol×K | 724.27 | Joback Calculated Property |
Cp,liquid | [161.10; 166.52] | J/mol×K | [298.15; 298.15] | |
T(K) Liquid phase heat capacity (J/mol×K) 161 162 163 164 165 166 167 | ||||
Cp,liquid | 161.10 | J/mol×K | 298.15 | NIST |
Cp,liquid | 166.24 | J/mol×K | 298.15 | NIST |
Cp,liquid | 165.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 166.52 | J/mol×K | 298.15 | NIST |
Cp,liquid | 165.20 | J/mol×K | 298.15 | NIST |
Cp,liquid | 165.20 | J/mol×K | 298.15 | NIST |
η | [0.0010010; 0.0011710] | Pa×s | [298.15; 313.15] | |
η | 0.0011710 | Pa×s | 298.15 | Excess ... |
η | 0.0011260 | Pa×s | 303.15 | Excess ... |
η | 0.0010680 | Pa×s | 308.15 | Excess ... |
η | 0.0010010 | Pa×s | 313.15 | Excess ... |
ΔfusH | [10.98; 10.98] | kJ/mol | [260.30; 260.33] | |
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 10 10.5 11 11.5 12 260.3 260.31 260.32 260.33000000000004 | ||||
ΔfusH | 10.98 | kJ/mol | 260.30 | NIST |
ΔfusH | 10.98 | kJ/mol | 260.30 | NIST |
ΔfusH | 10.98 | kJ/mol | 260.33 | NIST |
ΔfusH | 10.98 | kJ/mol | 260.33 | NIST |
ΔfusH | 10.98 | kJ/mol | 260.33 | NIST |
ΔvapH | [47.45; 49.10] | kJ/mol | [382.50; 464.10] | |
ΔvapH | 49.10 | kJ/mol | 382.50 | NIST |
ΔvapH | 47.45 | kJ/mol | 464.10 | KDB |
n0 | [1.52890; 1.53210] | [277.43; 284.13] | ||
T(K) Refractive Index 1.53 1.53 1.53 1.53 1.53 1.53 1.53 278 280 282 284 | ||||
n0 | 1.53210 | 277.43 | The mea... | |
n0 | 1.53180 | 278.33 | The mea... | |
n0 | 1.53120 | 279.49 | The mea... | |
n0 | 1.53070 | 280.36 | The mea... | |
n0 | 1.53070 | 280.38 | The mea... | |
n0 | 1.53050 | 280.86 | The mea... | |
n0 | 1.52990 | 281.97 | The mea... | |
n0 | 1.52890 | 284.13 | The mea... | |
ρl | [977.90; 1013.99] | kg/m3 | [283.15; 323.15] | |
T(K) Liquid Density (kg/m3) 980 990 1000 1010 290 300 310 320 | ||||
ρl | 1013.99 | kg/m3 | 283.15 | Measure... |
ρl | 1012.21 | kg/m3 | 285.15 | Measure... |
ρl | 1010.00 | kg/m3 | 288.00 | KDB |
ρl | 1009.55 | kg/m3 | 288.15 | Measure... |
ρl | 1005.12 | kg/m3 | 293.15 | Measure... |
ρl | 1000.60 | kg/m3 | 298.15 | Thermop... |
ρl | 1000.69 | kg/m3 | 298.15 | Measure... |
ρl | 996.26 | kg/m3 | 303.15 | Measure... |
ρl | 995.90 | kg/m3 | 303.15 | Thermop... |
ρl | 991.83 | kg/m3 | 308.15 | Measure... |
ρl | 991.40 | kg/m3 | 308.15 | Thermop... |
ρl | 987.40 | kg/m3 | 313.15 | Measure... |
ρl | 986.90 | kg/m3 | 313.15 | Thermop... |
ρl | 982.50 | kg/m3 | 318.15 | Thermop... |
ρl | 982.96 | kg/m3 | 318.15 | Measure... |
ρl | 977.90 | kg/m3 | 323.15 | Thermop... |
ΔfusS | [42.16; 42.16] | J/mol×K | [260.33; 260.33] | |
ΔfusS | 42.16 | J/mol×K | 260.33 | NIST |
ΔfusS | 42.16 | J/mol×K | 260.33 | NIST |
ΔfusS | 42.16 | J/mol×K | 260.33 | NIST |
csound,fluid | [1352.90; 1436.90] | m/s | [293.15; 318.15] | |
T(K) Speed of sound in fluid (m/s) 1360 1380 1400 1420 1440 300 310 | ||||
csound,fluid | 1436.90 | m/s | 293.15 | Densiti... |
csound,fluid | 1418.20 | m/s | 298.15 | Densiti... |
csound,fluid | 1400.70 | m/s | 303.15 | Densiti... |
csound,fluid | 1384.00 | m/s | 308.15 | Densiti... |
csound,fluid | 1368.20 | m/s | 313.15 | Densiti... |
csound,fluid | 1352.90 | m/s | 318.15 | Densiti... |
γ | 0.04 | N/m | 293.20 | KDB |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 342.00 | K | 1.30 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.66] | kPa | [341.12; 493.91] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.49604e+01 | |||
Coefficient B | -4.30561e+03 | |||
Coefficient C | -4.76780e+01 | |||
Temperature range, min. | 341.12 | |||
Temperature range, max. | 493.91 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
Pvap | 1.33 | kPa | 341.12 | Calculated Property |
Pvap | 2.97 | kPa | 358.10 | Calculated Property |
Pvap | 6.11 | kPa | 375.07 | Calculated Property |
Pvap | 11.68 | kPa | 392.05 | Calculated Property |
Pvap | 21.01 | kPa | 409.03 | Calculated Property |
Pvap | 35.86 | kPa | 426.00 | Calculated Property |
Pvap | 58.46 | kPa | 442.98 | Calculated Property |
Pvap | 91.55 | kPa | 459.96 | Calculated Property |
Pvap | 138.37 | kPa | 476.93 | Calculated Property |
Pvap | 202.66 | kPa | 493.91 | Calculated Property |
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