Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3500 | KDB | |
PAff | 825.80 | kJ/mol | NIST |
BasG | 794.80 | kJ/mol | NIST |
ΔcH°liquid | -2069.40 ± 0.67 | kJ/mol | NIST |
ΔfG° | -163.28 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -333.00 | kJ/mol | NIST |
ΔfH°liquid | -362.20 | kJ/mol | NIST |
ΔfusH° | 7.62 | kJ/mol | Joback Calculated Property |
ΔvapH° | [29.20; 29.20] | kJ/mol | |
ΔvapH° | 29.20 | kJ/mol | NIST |
ΔvapH° | 29.20 | kJ/mol | NIST |
IE | [9.90; 10.74] | eV | |
IE | 9.90 | eV | NIST |
IE | 10.74 | eV | NIST |
IE | 10.72 | eV | NIST |
log10WS | [-0.22; -0.22] | ||
log10WS | -0.22 | Aq. Sol... | |
log10WS | -0.22 | Estimat... | |
logPoct/wat | 0.345 | Crippen Calculated Property | |
McVol | 70.360 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 2 | KDB | |
NFPA Safety | 2 | KDB | |
Pc | 4300.00 | kPa | KDB |
Inp | [566.00; 625.00] | ||
Inp | 597.00 | NIST | |
Inp | 598.00 | NIST | |
Inp | 602.00 | NIST | |
Inp | 595.00 | NIST | |
Inp | 568.00 | NIST | |
Inp | 574.00 | NIST | |
Inp | 603.00 | NIST | |
Inp | 569.00 | NIST | |
Inp | 569.00 | NIST | |
Inp | 625.00 | NIST | |
Inp | 591.00 | NIST | |
Inp | 607.00 | NIST | |
Inp | 599.00 | NIST | |
Inp | 566.00 | NIST | |
Inp | 607.00 | NIST | |
Inp | 625.00 | NIST | |
Inp | 625.00 | NIST | |
I | [937.00; 941.00] | ||
I | 940.00 | NIST | |
I | 941.00 | NIST | |
I | 937.00 | NIST | |
I | 938.00 | NIST | |
I | 938.00 | NIST | |
Tboil | [353.00; 354.10] | K | |
Tboil | 353.50 | K | KDB |
Tboil | 353.70 | K | NIST |
Tboil | 353.00 | K | NIST |
Tboil | 354.10 ± 0.60 | K | NIST |
Tboil | 353.00 ± 2.00 | K | NIST |
Tc | 536.00 | K | KDB |
Tfus | [196.70; 197.77] | K | |
Tfus | 196.70 | K | KDB |
Tfus | 197.77 | K | Aq. Sol... |
Tfus | 197.50 | K | NIST |
Tfus | 197.50 ± 0.20 | K | NIST |
Vc | 0.265 | m3/kmol | KDB |
Zc | 0.2556890 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [116.32; 150.58] | J/mol×K | [363.89; 547.06] | |
T(K) Ideal gas heat capacity (J/mol×K) 115 120 125 130 135 140 145 150 400 450 500 550 | ||||
Cp,gas | 116.32 | J/mol×K | 363.89 | Joback Calculated Property |
Cp,gas | 122.50 | J/mol×K | 394.42 | Joback Calculated Property |
Cp,gas | 128.49 | J/mol×K | 424.95 | Joback Calculated Property |
Cp,gas | 134.29 | J/mol×K | 455.47 | Joback Calculated Property |
Cp,gas | 139.91 | J/mol×K | 486.00 | Joback Calculated Property |
Cp,gas | 145.34 | J/mol×K | 516.53 | Joback Calculated Property |
Cp,gas | 150.58 | J/mol×K | 547.06 | Joback Calculated Property |
Cp,liquid | [133.40; 172.30] | J/mol×K | [297.00; 298.15] | |
Cp,liquid | 133.40 | J/mol×K | 297.00 | NIST |
Cp,liquid | 172.30 | J/mol×K | 298.15 | NIST |
Cp,liquid | 161.50 | J/mol×K | 298.15 | NIST |
η | [0.0002583; 0.0021165] | Pa×s | [205.24; 363.89] | |
T(K) Dynamic viscosity (Pa×s) 5.00e-4 1.00e-3 1.50e-3 2.00e-3 250 300 350 | ||||
η | 0.0021165 | Pa×s | 205.24 | Joback Calculated Property |
η | 0.0012203 | Pa×s | 231.68 | Joback Calculated Property |
η | 0.0007877 | Pa×s | 258.12 | Joback Calculated Property |
η | 0.0005515 | Pa×s | 284.56 | Joback Calculated Property |
η | 0.0004102 | Pa×s | 311.01 | Joback Calculated Property |
η | 0.0003197 | Pa×s | 337.45 | Joback Calculated Property |
η | 0.0002583 | Pa×s | 363.89 | Joback Calculated Property |
ΔfusH | [9.73; 9.73] | kJ/mol | [197.50; 197.50] | |
ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
ΔfusH | 9.73 | kJ/mol | 197.50 | NIST |
ΔvapH | [28.80; 38.00] | kJ/mol | [291.00; 335.00] | |
ΔvapH | 38.00 | kJ/mol | 291.00 | NIST |
ΔvapH | 28.80 | kJ/mol | 318.00 | NIST |
ΔvapH | 34.20 | kJ/mol | 335.00 | NIST |
n0 | [1.39440; 1.40000] | [298.15; 313.15] | ||
n0 | 1.40000 | 298.15 | Volumet... | |
n0 | 1.39790 | 303.15 | Volumet... | |
n0 | 1.39540 | 308.15 | Volumet... | |
n0 | 1.39440 | 313.15 | Volumet... | |
ρl | [898.59; 973.52] | kg/m3 | [278.15; 338.15] | |
T(K) Liquid Density (kg/m3) 900 920 940 960 980 280 300 320 | ||||
ρl | 973.52 | kg/m3 | 278.15 | Thermop... |
ρl | 970.51 | kg/m3 | 280.65 | Thermop... |
ρl | 967.49 | kg/m3 | 283.15 | Thermop... |
ρl | 964.46 | kg/m3 | 285.65 | Thermop... |
ρl | 961.42 | kg/m3 | 288.15 | Thermop... |
ρl | 958.37 | kg/m3 | 290.65 | Thermop... |
ρl | 955.98 | kg/m3 | 293.00 | KDB |
ρl | 955.31 | kg/m3 | 293.15 | Thermop... |
ρl | 952.25 | kg/m3 | 295.65 | Thermop... |
ρl | 949.17 | kg/m3 | 298.15 | Self-ag... |
ρl | 947.56 | kg/m3 | 298.15 | Densiti... |
ρl | 949.17 | kg/m3 | 298.15 | Thermop... |
ρl | 946.10 | kg/m3 | 300.65 | Thermop... |
ρl | 943.00 | kg/m3 | 303.15 | Thermop... |
ρl | 939.91 | kg/m3 | 305.65 | Thermop... |
ρl | 936.80 | kg/m3 | 308.15 | Thermop... |
ρl | 933.68 | kg/m3 | 310.65 | Thermop... |
ρl | 930.55 | kg/m3 | 313.15 | Thermop... |
ρl | 927.41 | kg/m3 | 315.65 | Thermop... |
ρl | 924.25 | kg/m3 | 318.15 | Thermop... |
ρl | 921.09 | kg/m3 | 320.65 | Thermop... |
ρl | 917.91 | kg/m3 | 323.15 | Thermop... |
ρl | 914.73 | kg/m3 | 325.65 | Thermop... |
ρl | 911.53 | kg/m3 | 328.15 | Thermop... |
ρl | 908.31 | kg/m3 | 330.65 | Thermop... |
ρl | 905.09 | kg/m3 | 333.15 | Thermop... |
ρl | 901.85 | kg/m3 | 335.65 | Thermop... |
ρl | 898.59 | kg/m3 | 338.15 | Thermop... |
ΔfusS | 49.26 | J/mol×K | 197.50 | NIST |
csound,fluid | [1095.70; 1226.60] | m/s | [288.15; 318.15] | |
T(K) Speed of sound in fluid (m/s) 1100 1120 1140 1160 1180 1200 1220 290 300 310 | ||||
csound,fluid | 1226.60 | m/s | 288.15 | Ultraso... |
csound,fluid | 1204.60 | m/s | 293.15 | Ultraso... |
csound,fluid | 1183.60 | m/s | 298.15 | Ultraso... |
csound,fluid | 1162.20 | m/s | 303.15 | Ultraso... |
csound,fluid | 1139.10 | m/s | 308.15 | Ultraso... |
csound,fluid | 1117.80 | m/s | 313.15 | Ultraso... |
csound,fluid | 1095.70 | m/s | 318.15 | Ultraso... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [259.45; 376.82] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.47471e+01 | |||
Coefficient B | -3.18738e+03 | |||
Coefficient C | -3.90130e+01 | |||
Temperature range, min. | 259.45 | |||
Temperature range, max. | 376.82 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 259.45 | Calculated Property |
Pvap | 2.99 | kPa | 272.49 | Calculated Property |
Pvap | 6.16 | kPa | 285.53 | Calculated Property |
Pvap | 11.79 | kPa | 298.57 | Calculated Property |
Pvap | 21.21 | kPa | 311.61 | Calculated Property |
Pvap | 36.18 | kPa | 324.66 | Calculated Property |
Pvap | 58.89 | kPa | 337.70 | Calculated Property |
Pvap | 92.03 | kPa | 350.74 | Calculated Property |
Pvap | 138.75 | kPa | 363.78 | Calculated Property |
Pvap | 202.67 | kPa | 376.82 | Calculated Property |
Pvap | [4.11e-03; 4206.00] | kPa | [196.32; 536.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 6.86079e+01 | |||
Coefficient B | -6.30414e+03 | |||
Coefficient C | -7.99764e+00 | |||
Coefficient D | 6.11250e-06 | |||
Temperature range, min. | 196.32 | |||
Temperature range, max. | 536.00 | |||
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 200 300 400 500 | ||||
Pvap | 4.11e-03 | kPa | 196.32 | Calculated Property |
Pvap | 0.20 | kPa | 234.06 | Calculated Property |
Pvap | 2.82 | kPa | 271.80 | Calculated Property |
Pvap | 19.31 | kPa | 309.55 | Calculated Property |
Pvap | 81.88 | kPa | 347.29 | Calculated Property |
Pvap | 251.75 | kPa | 385.03 | Calculated Property |
Pvap | 619.30 | kPa | 422.77 | Calculated Property |
Pvap | 1300.58 | kPa | 460.52 | Calculated Property |
Pvap | 2437.46 | kPa | 498.26 | Calculated Property |
Pvap | 4206.00 | kPa | 536.00 | Calculated Property |
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