Property | Value | Unit | Source |
---|---|---|---|
ω | 0.2710 | KDB | |
AP | 309.850 | K | KDB |
ΔcH°liquid | [-4591.94; -4589.60] | kJ/mol | |
ΔcH°liquid | -4591.94 ± 0.92 | kJ/mol | NIST |
ΔcH°liquid | -4589.60 ± 1.50 | kJ/mol | NIST |
ΔfG° | 44.59 | kJ/mol | KDB |
Δc,grossH | 4591.94 | kJ/mol | KDB |
Δc,netH | 4283.872 | kJ/mol | KDB |
ΔfH°gas | [-129.40; -127.10] | kJ/mol | |
ΔfH°gas | -127.20 | kJ/mol | KDB |
ΔfH°gas | -127.10 ± 1.00 | kJ/mol | NIST |
ΔfH°gas | -129.40 | kJ/mol | NIST |
ΔfH°liquid | [-165.80; -163.50] | kJ/mol | |
ΔfH°liquid | -163.50 ± 1.00 | kJ/mol | NIST |
ΔfH°liquid | -165.80 ± 1.60 | kJ/mol | NIST |
ΔfusH° | 7.82 | kJ/mol | Joback Calculated Property |
ΔvapH° | [36.40; 36.50] | kJ/mol | |
ΔvapH° | 36.47 | kJ/mol | NIST |
ΔvapH° | 36.50 | kJ/mol | NIST |
ΔvapH° | 36.40 | kJ/mol | NIST |
IE | [9.60; 10.12] | eV | |
IE | 9.60 | eV | NIST |
IE | 10.12 ± 0.02 | eV | NIST |
log10WS | -2.41 | Crippen Calculated Property | |
logPoct/wat | 2.587 | Crippen Calculated Property | |
McVol | 98.630 | ml/mol | McGowan Calculated Property |
NFPA Fire | 3 | KDB | |
NFPA Health | 1 | KDB | |
Pc | [3397.02; 3400.00] | kPa | |
Pc | 3400.00 | kPa | KDB |
Pc | 3400.00 ± 40.00 | kPa | NIST |
Pc | 3397.02 ± 5.06 | kPa | NIST |
ρc | [262.16; 262.16] | kg/m3 | |
ρc | 262.16 ± 3.93 | kg/m3 | NIST |
ρc | 262.16 ± 1.96 | kg/m3 | NIST |
Inp | [711.00; 753.00] | ||
Inp | 722.00 | NIST | |
Inp | 741.50 | NIST | |
Inp | 729.00 | NIST | |
Inp | 734.30 | NIST | |
Inp | 734.50 | NIST | |
Inp | 734.80 | NIST | |
Inp | 734.80 | NIST | |
Inp | 733.80 | NIST | |
Inp | 737.50 | NIST | |
Inp | 734.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 733.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 733.10 | NIST | |
Inp | 737.00 | NIST | |
Inp | 733.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | 729.90 | NIST | |
Inp | 731.90 | NIST | |
Inp | 734.10 | NIST | |
Inp | 735.60 | NIST | |
Inp | 743.40 | NIST | |
Inp | 727.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 731.00 | NIST | |
Inp | 733.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 734.30 | NIST | |
Inp | 734.80 | NIST | |
Inp | Outlier 750.00 | NIST | |
Inp | 739.00 | NIST | |
Inp | 732.00 | NIST | |
Inp | 732.00 | NIST | |
Inp | 732.00 | NIST | |
Inp | 741.30 | NIST | |
Inp | 741.50 | NIST | |
Inp | 737.10 | NIST | |
Inp | 737.90 | NIST | |
Inp | 743.00 | NIST | |
Inp | 733.10 | NIST | |
Inp | 738.10 | NIST | |
Inp | 738.10 | NIST | |
Inp | 744.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | Outlier 748.00 | NIST | |
Inp | 743.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 742.00 | NIST | |
Inp | 734.40 | NIST | |
Inp | 734.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | Outlier 749.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | 741.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | Outlier 749.00 | NIST | |
Inp | 733.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 745.00 | NIST | |
Inp | 728.70 | NIST | |
Inp | 732.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | 731.00 | NIST | |
Inp | 732.00 | NIST | |
Inp | 725.65 | NIST | |
Inp | 726.06 | NIST | |
Inp | 724.50 | NIST | |
Inp | 733.30 | NIST | |
Inp | 729.70 | NIST | |
Inp | 726.90 | NIST | |
Inp | 726.98 | NIST | |
Inp | 727.03 | NIST | |
Inp | 727.17 | NIST | |
Inp | 727.00 | NIST | |
Inp | 732.40 | NIST | |
Inp | 729.10 | NIST | |
Inp | 728.50 | NIST | |
Inp | 725.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 732.00 | NIST | |
Inp | 735.00 | NIST | |
Inp | Outlier 711.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 731.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 727.00 | NIST | |
Inp | 730.00 | NIST | |
Inp | 727.00 | NIST | |
Inp | 729.00 | NIST | |
Inp | Outlier 749.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | Outlier 751.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 736.00 | NIST | |
Inp | 739.00 | NIST | |
Inp | 728.00 | NIST | |
Inp | 726.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 734.00 | NIST | |
Inp | 725.00 | NIST | |
Inp | 733.00 | NIST | |
Inp | 739.00 | NIST | |
Inp | Outlier 753.00 | NIST | |
Inp | 722.00 | NIST | |
Inp | 734.80 | NIST | |
Inp | 735.00 | NIST | |
Inp | 737.00 | NIST | |
Inp | 731.90 | NIST | |
Inp | 729.00 | NIST | |
Inp | 734.30 | NIST | |
Inp | 732.00 | NIST | |
Inp | 737.90 | NIST | |
Inp | 744.00 | NIST | |
Inp | Outlier 748.00 | NIST | |
Inp | 740.00 | NIST | |
Inp | 738.00 | NIST | |
Inp | Outlier 749.00 | NIST | |
I | [773.00; 817.00] | ||
I | 817.00 | NIST | |
I | 801.00 | NIST | |
I | 809.00 | NIST | |
I | 817.00 | NIST | |
I | 773.00 | NIST | |
S°gas | 378.32 | J/mol×K | NIST |
S°liquid | 279.91 | J/mol×K | NIST |
Tboil | 376.60 | K | KDB |
Tc | [569.45; 569.50] | K | |
Tc | 569.50 | K | KDB |
Tc | 569.50 ± 0.50 | K | NIST |
Tc | 569.50 | K | NIST |
Tc | 569.45 ± 0.05 | K | NIST |
Tfus | 134.71 | K | KDB |
Vc | [0.375; 0.375] | m3/kmol | |
Vc | 0.375 | m3/kmol | KDB |
Vc | 0.375 | m3/kmol | NIST |
Zc | 0.2692650 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [173.92; 255.21] | J/mol×K | [374.84; 568.84] | |
T(K) Ideal gas heat capacity (J/mol×K) 180 200 220 240 260 400 450 500 550 | ||||
Cp,gas | 173.92 | J/mol×K | 374.84 | Joback Calculated Property |
Cp,gas | 189.22 | J/mol×K | 407.17 | Joback Calculated Property |
Cp,gas | 203.78 | J/mol×K | 439.51 | Joback Calculated Property |
Cp,gas | 217.64 | J/mol×K | 471.84 | Joback Calculated Property |
Cp,gas | 230.81 | J/mol×K | 504.17 | Joback Calculated Property |
Cp,gas | 243.33 | J/mol×K | 536.50 | Joback Calculated Property |
Cp,gas | 255.21 | J/mol×K | 568.84 | Joback Calculated Property |
Cp,liquid | 187.61 | J/mol×K | 301.83 | NIST |
η | [0.0002960; 0.0038089] | Pa×s | [179.55; 374.84] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 3.00e-3 3.50e-3 4.00e-3 200 250 300 350 | ||||
η | 0.0038089 | Pa×s | 179.55 | Joback Calculated Property |
η | 0.0017947 | Pa×s | 212.10 | Joback Calculated Property |
η | 0.0010331 | Pa×s | 244.65 | Joback Calculated Property |
η | 0.0006770 | Pa×s | 277.19 | Joback Calculated Property |
η | 0.0004849 | Pa×s | 309.74 | Joback Calculated Property |
η | 0.0003701 | Pa×s | 342.29 | Joback Calculated Property |
η | 0.0002960 | Pa×s | 374.84 | Joback Calculated Property |
ΔfusH | [6.86; 6.87] | kJ/mol | [134.70; 134.70] | |
ΔfusH | 6.86 | kJ/mol | 134.70 | NIST |
ΔfusH | 6.87 | kJ/mol | 134.70 | NIST |
ΔvapH | [31.90; 35.70] | kJ/mol | [313.00; 534.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 33 34 35 36 350 400 450 500 | ||||
ΔvapH | 35.60 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 34.80 ± 0.10 | kJ/mol | 328.00 | NIST |
ΔvapH | 35.70 | kJ/mol | 339.50 | NIST |
ΔvapH | 33.90 ± 0.10 | kJ/mol | 343.00 | NIST |
ΔvapH | 35.50 | kJ/mol | 347.50 | NIST |
ΔvapH | 33.00 ± 0.10 | kJ/mol | 358.00 | NIST |
ΔvapH | 32.50 ± 0.10 | kJ/mol | 368.00 | NIST |
ΔvapH | 32.28 | kJ/mol | 376.60 | KDB |
ΔvapH | 31.96 | kJ/mol | 376.60 | NIST |
ΔvapH | 32.90 | kJ/mol | 446.50 | NIST |
ΔvapH | 31.90 | kJ/mol | 534.00 | NIST |
n0 | 1.41730 | 298.15 | KDB | |
ρl | 771.00 | kg/m3 | 289.00 | KDB |
γ | 0.02 | N/m | 293.20 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [271.79; 402.74] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43149e+01 | |||
Coefficient B | -3.29180e+03 | |||
Coefficient C | -3.71200e+01 | |||
Temperature range, min. | 271.79 | |||
Temperature range, max. | 402.74 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 400 | ||||
Pvap | 1.33 | kPa | 271.79 | Calculated Property |
Pvap | 3.02 | kPa | 286.34 | Calculated Property |
Pvap | 6.27 | kPa | 300.89 | Calculated Property |
Pvap | 12.03 | kPa | 315.44 | Calculated Property |
Pvap | 21.65 | kPa | 329.99 | Calculated Property |
Pvap | 36.86 | kPa | 344.54 | Calculated Property |
Pvap | 59.80 | kPa | 359.09 | Calculated Property |
Pvap | 93.04 | kPa | 373.64 | Calculated Property |
Pvap | 139.55 | kPa | 388.19 | Calculated Property |
Pvap | 202.67 | kPa | 402.74 | Calculated Property |
Pvap | [3.71e-09; 3377.64] | kPa | [134.71; 569.52] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.15619e+01 | |||
Coefficient B | -7.00763e+03 | |||
Coefficient C | -1.00117e+01 | |||
Coefficient D | 7.36714e-06 | |||
Temperature range, min. | 134.71 | |||
Temperature range, max. | 569.52 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 200 300 400 500 | ||||
Pvap | 3.71e-09 | kPa | 134.71 | Calculated Property |
Pvap | 1.77e-04 | kPa | 183.02 | Calculated Property |
Pvap | 0.06 | kPa | 231.33 | Calculated Property |
Pvap | 1.97 | kPa | 279.65 | Calculated Property |
Pvap | 19.89 | kPa | 327.96 | Calculated Property |
Pvap | 100.35 | kPa | 376.27 | Calculated Property |
Pvap | 331.45 | kPa | 424.58 | Calculated Property |
Pvap | 837.27 | kPa | 472.90 | Calculated Property |
Pvap | 1778.76 | kPa | 521.21 | Calculated Property |
Pvap | 3377.64 | kPa | 569.52 | Calculated Property |
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