Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3960 | KDB | |
PAff | 648.00 | kJ/mol | NIST |
BasG | 624.40 | kJ/mol | NIST |
ΔcH°liquid | [-2443.60; -2041.00] | kJ/mol | |
ΔcH°liquid | -2041.00 ± 8.40 | kJ/mol | NIST |
ΔcH°liquid | -2443.60 ± 1.20 | kJ/mol | NIST |
Cp,liquid | 221.42 | J/mol×K | Reassem... |
EA | [0.48; 1.80] | eV | |
EA | 0.53 ± 0.05 | eV | NIST |
EA | 0.52 ± 0.11 | eV | NIST |
EA | 0.70 ± 0.10 | eV | NIST |
EA | 0.48 | eV | NIST |
EA | 0.80 ± 0.10 | eV | NIST |
EA | 0.83 ± 0.20 | eV | NIST |
EA | 0.86 ± 0.03 | eV | NIST |
EA | Outlier 1.80 ± 0.30 | eV | NIST |
EA | 1.20 ± 0.07 | eV | NIST |
ΔfG° | -880.00 | kJ/mol | KDB |
ΔfH°gas | [-957.30; -956.00] | kJ/mol | |
ΔfH°gas | -957.30 | kJ/mol | KDB |
ΔfH°gas | -956.00 ± 1.20 | kJ/mol | NIST |
ΔfH°liquid | -991.70 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 21.87 | kJ/mol | Joback Calculated Property |
ΔvapH° | 29.63 | kJ/mol | Joback Calculated Property |
IE | [9.80; 10.20] | eV | |
IE | 9.90 ± 0.04 | eV | NIST |
IE | 9.80 | eV | NIST |
IE | 9.91 | eV | NIST |
IE | 9.90 ± 0.05 | eV | NIST |
IE | 9.91 | eV | NIST |
IE | 10.20 ± 0.10 | eV | NIST |
IE | 9.93 | eV | NIST |
IE | 9.90 ± 0.01 | eV | NIST |
IE | 9.88 ± 0.05 | eV | NIST |
IE | 9.97 | eV | NIST |
IE | 10.20 | eV | NIST |
IE | 10.14 | eV | NIST |
IE | 10.09 | eV | NIST |
IE | 10.09 | eV | NIST |
IE | 9.90 | eV | NIST |
log10WS | -3.46 | Crippen Calculated Property | |
logPoct/wat | 2.521 | Crippen Calculated Property | |
McVol | 82.260 | ml/mol | McGowan Calculated Property |
Pc | 3273.00 | kPa | KDB |
ρc | [493.04; 550.35] | kg/m3 | |
ρc | 550.35 ± 0.54 | kg/m3 | NIST |
ρc | 493.04 ± 4.91 | kg/m3 | NIST |
Inp | [546.80; 609.00] | ||
Inp | 546.80 | NIST | |
Inp | 548.70 | NIST | |
Inp | 576.00 | NIST | |
Inp | 571.00 | NIST | |
Inp | 569.00 | NIST | |
Inp | 600.00 | NIST | |
Inp | 592.00 | NIST | |
Inp | 609.00 | NIST | |
Inp | 600.00 | NIST | |
S°liquid | [279.91; 280.79] | J/mol×K | |
S°liquid | 280.79 | J/mol×K | NIST |
S°liquid | 279.91 | J/mol×K | NIST |
Tboil | 353.41 | K | KDB |
Tc | 516.73 | K | KDB |
Tfus | 278.50 | K | KDB |
Ttriple | [278.14; 278.30] | K | |
Ttriple | 278.30 | K | KDB |
Ttriple | 278.30 ± 0.02 | K | NIST |
Ttriple | 278.14 ± 0.15 | K | NIST |
Ttriple | 278.25 ± 0.02 | K | NIST |
Vc | [0.335; 0.335] | m3/kmol | |
Vc | 0.335 | m3/kmol | KDB |
Vc | 0.335 ± 0.002 | m3/kmol | NIST |
Zc | 0.2552060 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [159.94; 187.66] | J/mol×K | [383.88; 542.33] | |
T(K) Ideal gas heat capacity (J/mol×K) 160 165 170 175 180 185 190 400 450 500 | ||||
Cp,gas | 159.94 | J/mol×K | 383.88 | Joback Calculated Property |
Cp,gas | 164.92 | J/mol×K | 410.29 | Joback Calculated Property |
Cp,gas | 169.76 | J/mol×K | 436.70 | Joback Calculated Property |
Cp,gas | 174.45 | J/mol×K | 463.10 | Joback Calculated Property |
Cp,gas | 179.00 | J/mol×K | 489.51 | Joback Calculated Property |
Cp,gas | 183.41 | J/mol×K | 515.92 | Joback Calculated Property |
Cp,gas | 187.66 | J/mol×K | 542.33 | Joback Calculated Property |
Cp,liquid | [221.30; 225.03] | J/mol×K | [298.15; 300.00] | |
T(K) Liquid phase heat capacity (J/mol×K) 221 222 223 224 225 298.5 299 299.5 300 | ||||
Cp,liquid | 225.03 | J/mol×K | 298.15 | NIST |
Cp,liquid | 221.60 | J/mol×K | 298.15 | NIST |
Cp,liquid | 221.58 | J/mol×K | 298.15 | NIST |
Cp,liquid | 221.58 | J/mol×K | 298.15 | NIST |
Cp,liquid | 221.30 | J/mol×K | 298.76 | NIST |
Cp,liquid | 222.00 | J/mol×K | 300.00 | NIST |
ΔfusH | [11.59; 11.59] | kJ/mol | [278.25; 278.30] | |
ΔfusH | 11.59 | kJ/mol | 278.25 | NIST |
ΔfusH | 11.59 | kJ/mol | 278.30 | NIST |
ΔfusH | 11.59 | kJ/mol | 278.30 | NIST |
ΔfusH | 11.59 | kJ/mol | 278.30 | NIST |
ΔsubH | [46.00; 49.80] | kJ/mol | [246.50; 316.00] | |
ΔsubH | 49.20 | kJ/mol | 246.50 | NIST |
ΔsubH | 49.80 | kJ/mol | 253.00 | NIST |
ΔsubH | 46.00 | kJ/mol | 316.00 | NIST |
ΔvapH | [31.66; 36.50] | kJ/mol | [299.50; 487.50] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 32 33 34 35 36 300 350 400 450 | ||||
ΔvapH | 36.20 | kJ/mol | 299.50 | NIST |
ΔvapH | 35.70 | kJ/mol | 308.00 | NIST |
ΔvapH | 36.50 | kJ/mol | 316.00 | NIST |
ΔvapH | 35.10 | kJ/mol | 324.50 | NIST |
ΔvapH | 35.50 | kJ/mol | 325.50 | NIST |
ΔvapH | 36.50 | kJ/mol | 331.00 | NIST |
ΔvapH | 34.40 | kJ/mol | 347.00 | NIST |
ΔvapH | 31.66 | kJ/mol | 353.30 | NIST |
ΔvapH | 31.68 | kJ/mol | 353.40 | KDB |
ΔvapH | 33.20 | kJ/mol | 368.50 | NIST |
ΔvapH | 32.20 | kJ/mol | 423.00 | NIST |
ΔvapH | 32.20 | kJ/mol | 439.50 | NIST |
ΔvapH | 31.80 | kJ/mol | 459.50 | NIST |
ΔvapH | 31.80 | kJ/mol | 487.50 | NIST |
ν | [0.0000004; 0.0000006] | m2/s | [298.15; 318.15] | |
T(K) Kinematic viscosity (m2/s) 4.50e-7 5.00e-7 5.50e-7 300 305 310 315 | ||||
ν | 0.0000006 | m2/s | 298.15 | Viscosi... |
ν | 0.0000005 | m2/s | 303.15 | Viscosi... |
ν | 0.0000005 | m2/s | 308.15 | Viscosi... |
ν | 0.0000004 | m2/s | 313.15 | Viscosi... |
ν | 0.0000004 | m2/s | 318.15 | Viscosi... |
Pvap | [6.90; 49.95] | kPa | [288.23; 333.01] | |
T(K) Vapor pressure (kPa) 10 20 30 40 50 300 320 | ||||
Pvap | 6.90 | kPa | 288.23 | Densiti... |
Pvap | 9.00 | kPa | 293.51 | Densiti... |
Pvap | 11.16 | kPa | 297.98 | Densiti... |
Pvap | 14.20 | kPa | 302.96 | Densiti... |
Pvap | 17.93 | kPa | 307.96 | Densiti... |
Pvap | 22.25 | kPa | 312.96 | Densiti... |
Pvap | 27.56 | kPa | 317.96 | Densiti... |
Pvap | 33.85 | kPa | 322.96 | Densiti... |
Pvap | 41.16 | kPa | 327.95 | Densiti... |
Pvap | 49.95 | kPa | 333.01 | Densiti... |
ρl | [610.10; 1605.40] | kg/m3 | [298.79; 516.57] | |
T(K) Liquid Density (kg/m3) 600 800 1000 1200 1400 1600 300 400 500 | ||||
ρl | 1605.40 | kg/m3 | 298.79 | Propert... |
ρl | 1548.50 | kg/m3 | 323.83 | Propert... |
ρl | 1499.40 | kg/m3 | 343.88 | Propert... |
ρl | 1450.50 | kg/m3 | 363.85 | Propert... |
ρl | 1397.90 | kg/m3 | 383.91 | Propert... |
ρl | 1342.10 | kg/m3 | 403.92 | Propert... |
ρl | 1281.20 | kg/m3 | 423.93 | Propert... |
ρl | 1213.90 | kg/m3 | 443.90 | Propert... |
ρl | 1135.30 | kg/m3 | 463.89 | Propert... |
ρl | 1037.10 | kg/m3 | 483.90 | Propert... |
ρl | 974.00 | kg/m3 | 493.93 | Propert... |
ρl | 892.30 | kg/m3 | 503.88 | Propert... |
ρl | 835.80 | kg/m3 | 508.90 | Propert... |
ρl | 744.60 | kg/m3 | 513.91 | Propert... |
ρl | 746.30 | kg/m3 | 513.92 | Propert... |
ρl | 670.30 | kg/m3 | 515.98 | Propert... |
ρl | 644.80 | kg/m3 | 516.28 | Propert... |
ρl | 610.10 | kg/m3 | 516.57 | Propert... |
ΔfusS | [41.63; 41.65] | J/mol×K | [278.25; 278.30] | |
ΔfusS | 41.65 | J/mol×K | 278.25 | NIST |
ΔfusS | 41.63 | J/mol×K | 278.30 | NIST |
γ | [0.02; 0.02] | N/m | [288.05; 318.75] | |
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 290 300 310 | ||||
γ | 0.02 | N/m | 288.05 | Surface... |
γ | 0.02 | N/m | 293.35 | Surface... |
γ | 0.02 | N/m | 298.45 | Surface... |
γ | 0.02 | N/m | 303.45 | Surface... |
γ | 0.02 | N/m | 308.55 | Surface... |
γ | 0.02 | N/m | 313.65 | Surface... |
γ | 0.02 | N/m | 318.75 | Surface... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | [354.50; 354.70] | K | [99.10; 99.10] | |
Tboilr | 354.70 | K | 99.10 | NIST |
Tboilr | 354.50 ± 0.50 | K | 99.10 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.63] | kPa | [266.07; 377.60] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.38550e+01 | |||
Coefficient B | -2.57337e+03 | |||
Coefficient C | -7.63960e+01 | |||
Temperature range, min. | 266.07 | |||
Temperature range, max. | 377.60 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 266.07 | Calculated Property |
Pvap | 3.06 | kPa | 278.46 | Calculated Property |
Pvap | 6.40 | kPa | 290.85 | Calculated Property |
Pvap | 12.32 | kPa | 303.25 | Calculated Property |
Pvap | 22.17 | kPa | 315.64 | Calculated Property |
Pvap | 37.65 | kPa | 328.03 | Calculated Property |
Pvap | 60.85 | kPa | 340.42 | Calculated Property |
Pvap | 94.19 | kPa | 352.82 | Calculated Property |
Pvap | 140.44 | kPa | 365.21 | Calculated Property |
Pvap | 202.63 | kPa | 377.60 | Calculated Property |
Pvap | [3.84; 3263.58] | kPa | [278.00; 516.73] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 9.63466e+01 | |||
Coefficient B | -7.45555e+03 | |||
Coefficient C | -1.22574e+01 | |||
Coefficient D | 1.03019e-05 | |||
Temperature range, min. | 278.00 | |||
Temperature range, max. | 516.73 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 3500 300 400 500 | ||||
Pvap | 3.84 | kPa | 278.00 | Calculated Property |
Pvap | 15.22 | kPa | 304.53 | Calculated Property |
Pvap | 46.25 | kPa | 331.05 | Calculated Property |
Pvap | 115.36 | kPa | 357.58 | Calculated Property |
Pvap | 248.01 | kPa | 384.10 | Calculated Property |
Pvap | 476.26 | kPa | 410.63 | Calculated Property |
Pvap | 838.86 | kPa | 437.15 | Calculated Property |
Pvap | 1382.70 | kPa | 463.68 | Calculated Property |
Pvap | 2165.99 | kPa | 490.20 | Calculated Property |
Pvap | 3263.58 | kPa | 516.73 | Calculated Property |
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