Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3230 | KDB | |
AP | 343.650 | K | KDB |
ΔcH°liquid | [-4813.90; -4813.00] | kJ/mol | |
ΔcH°liquid | -4813.90 ± 1.20 | kJ/mol | NIST |
ΔcH°liquid | -4813.00 ± 1.00 | kJ/mol | NIST |
μ | 0.00 | debye | KDB |
ΔfG° | 4.60 | kJ/mol | KDB |
Δc,grossH | 4813.90 | kJ/mol | KDB |
Δc,netH | 4461.776 | kJ/mol | KDB |
ΔfH°gas | [-192.90; -192.30] | kJ/mol | |
ΔfH°gas | -192.40 | kJ/mol | KDB |
ΔfH°gas | -192.30 ± 1.30 | kJ/mol | NIST |
ΔfH°gas | -192.90 | kJ/mol | NIST |
ΔfH°liquid | [-228.00; -227.40] | kJ/mol | |
ΔfH°liquid | -227.40 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -228.00 ± 1.00 | kJ/mol | NIST |
ΔfusH° | 10.36 | kJ/mol | Joback Calculated Property |
ΔvapH° | [35.10; 35.16] | kJ/mol | |
ΔvapH° | 35.16 | kJ/mol | NIST |
ΔvapH° | 35.10 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 35.10 | kJ/mol | NIST |
log10WS | -2.51 | Crippen Calculated Property | |
logPoct/wat | 2.833 | Crippen Calculated Property | |
McVol | 109.490 | ml/mol | McGowan Calculated Property |
Pc | [2810.00; 2850.00] | kPa | |
Pc | 2810.00 | kPa | KDB |
Pc | 2810.00 ± 40.00 | kPa | NIST |
Pc | 2813.50 ± 40.53 | kPa | NIST |
Pc | 2850.00 ± 5133.40 | kPa | NIST |
ρc | [247.50; 248.50] | kg/m3 | |
ρc | 247.50 ± 4.01 | kg/m3 | NIST |
ρc | 248.50 ± 5.01 | kg/m3 | NIST |
Inp | [664.00; 689.20] | ||
Inp | 675.90 | NIST | |
Inp | 676.60 | NIST | |
Inp | 676.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.20 | NIST | |
Inp | Outlier 689.20 | NIST | |
Inp | 675.50 | NIST | |
Inp | 679.30 | NIST | |
Inp | Outlier 682.30 | NIST | |
Inp | 675.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 675.80 | NIST | |
Inp | 676.80 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 675.70 | NIST | |
Inp | 676.10 | NIST | |
Inp | 676.40 | NIST | |
Inp | 676.90 | NIST | |
Inp | 674.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.80 | NIST | |
Inp | 676.80 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 675.50 | NIST | |
Inp | 676.10 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 678.50 | NIST | |
Inp | 671.10 | NIST | |
Inp | 673.20 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.51 | NIST | |
Inp | 679.09 | NIST | |
Inp | 679.75 | NIST | |
Inp | 677.32 | NIST | |
Inp | 677.95 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.40 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | Outlier 683.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 679.00 | NIST | |
Inp | Outlier 667.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 675.80 | NIST | |
Inp | 678.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 673.90 | NIST | |
Inp | Outlier 666.92 | NIST | |
Inp | Outlier 667.66 | NIST | |
Inp | 672.70 | NIST | |
Inp | 672.20 | NIST | |
Inp | 670.16 | NIST | |
Inp | 670.26 | NIST | |
Inp | 676.00 | NIST | |
Inp | 670.56 | NIST | |
Inp | 670.60 | NIST | |
Inp | 671.00 | NIST | |
Inp | 676.90 | NIST | |
Inp | 676.50 | NIST | |
Inp | 675.80 | NIST | |
Inp | 669.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 669.20 | NIST | |
Inp | 672.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 669.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | Outlier 664.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 672.20 | NIST | |
Inp | 670.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 678.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | Outlier 668.04 | NIST | |
Inp | 672.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | 676.00 | NIST | |
Inp | 677.00 | NIST | |
Inp | Outlier 665.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 674.00 | NIST | |
Inp | 672.00 | NIST | |
Inp | 673.00 | NIST | |
Inp | 675.00 | NIST | |
Inp | Outlier 683.00 | NIST | |
Inp | Outlier 685.00 | NIST | |
Inp | Outlier 683.00 | NIST | |
Inp | Outlier 685.00 | NIST | |
Inp | 671.00 | NIST | |
Inp | 672.20 | NIST | |
Inp | 670.60 | NIST | |
Inp | 669.00 | NIST | |
Inp | Outlier 667.00 | NIST | |
Inp | 675.80 | NIST | |
I | 700.00 | NIST | |
S°liquid | 309.60 | J/mol×K | NIST |
Tboil | 364.99 | K | KDB |
Tc | [535.19; 535.55] | K | |
Tc | 535.20 | K | KDB |
Tc | 535.20 ± 0.40 | K | NIST |
Tc | 535.20 | K | NIST |
Tc | 535.19 ± 0.40 | K | NIST |
Tc | 535.55 ± 0.50 | K | NIST |
Tfus | [153.70; 153.75] | K | |
Tfus | 153.70 | K | KDB |
Tfus | 153.75 ± 0.50 | K | NIST |
Vc | [0.404; 0.404] | m3/kmol | |
Vc | 0.404 | m3/kmol | KDB |
Vc | 0.404 | m3/kmol | NIST |
Zc | 0.2551140 | KDB | |
Zra | 0.27 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [194.02; 260.72] | J/mol×K | [359.12; 526.54] | |
T(K) Ideal gas heat capacity (J/mol×K) 190 200 210 220 230 240 250 260 400 450 500 | ||||
Cp,gas | 194.02 | J/mol×K | 359.12 | Joback Calculated Property |
Cp,gas | 206.19 | J/mol×K | 387.02 | Joback Calculated Property |
Cp,gas | 217.92 | J/mol×K | 414.93 | Joback Calculated Property |
Cp,gas | 229.23 | J/mol×K | 442.83 | Joback Calculated Property |
Cp,gas | 240.13 | J/mol×K | 470.73 | Joback Calculated Property |
Cp,gas | 250.62 | J/mol×K | 498.63 | Joback Calculated Property |
Cp,gas | 260.72 | J/mol×K | 526.54 | Joback Calculated Property |
Cp,liquid | [214.20; 216.70] | J/mol×K | [289.20; 289.20] | |
Cp,liquid | 216.70 | J/mol×K | 289.20 | NIST |
Cp,liquid | 214.20 | J/mol×K | 289.20 | NIST |
η | [0.0002348; 0.0099972] | Pa×s | [153.65; 359.12] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 200 300 | ||||
η | 0.0099972 | Pa×s | 153.65 | Joback Calculated Property |
η | 0.0030264 | Pa×s | 187.90 | Joback Calculated Property |
η | 0.0013243 | Pa×s | 222.14 | Joback Calculated Property |
η | 0.0007226 | Pa×s | 256.38 | Joback Calculated Property |
η | 0.0004548 | Pa×s | 290.63 | Joback Calculated Property |
η | 0.0003156 | Pa×s | 324.88 | Joback Calculated Property |
η | 0.0002348 | Pa×s | 359.12 | Joback Calculated Property |
ΔvapH | [30.79; 35.10] | kJ/mol | [313.00; 365.00] | |
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 31 32 33 34 35 320 340 360 | ||||
ΔvapH | 34.20 ± 0.10 | kJ/mol | 313.00 | NIST |
ΔvapH | 35.10 | kJ/mol | 327.50 | NIST |
ΔvapH | 34.90 | kJ/mol | 329.50 | NIST |
ΔvapH | 32.90 ± 0.10 | kJ/mol | 333.00 | NIST |
ΔvapH | 31.70 ± 0.10 | kJ/mol | 353.00 | NIST |
ΔvapH | 30.89 | kJ/mol | 365.00 | NIST |
ΔvapH | 30.79 | kJ/mol | 365.00 | KDB |
n0 | 1.38609 | 298.15 | KDB | |
ρl | 687.00 | kg/m3 | 293.00 | KDB |
γ | 0.02 | N/m | 298.20 | KDB |
λ | [0.10; 0.12] | W/m×K | [256.62; 344.30] | |
T(K) Liquid thermal conductivity (W/m×K) 0.1 0.11 0.11 0.12 0.12 0.13 300 | ||||
λ | 0.12 | W/m×K | 256.62 | Thermal... |
λ | 0.12 | W/m×K | 257.00 | Thermal... |
λ | 0.12 | W/m×K | 257.38 | Thermal... |
λ | 0.12 | W/m×K | 269.72 | Thermal... |
λ | 0.12 | W/m×K | 270.11 | Thermal... |
λ | 0.12 | W/m×K | 270.44 | Thermal... |
λ | 0.12 | W/m×K | 284.90 | Thermal... |
λ | 0.11 | W/m×K | 285.32 | Thermal... |
λ | 0.11 | W/m×K | 285.66 | Thermal... |
λ | 0.11 | W/m×K | 296.55 | Thermal... |
λ | 0.11 | W/m×K | 296.95 | Thermal... |
λ | 0.11 | W/m×K | 297.35 | Thermal... |
λ | 0.11 | W/m×K | 311.54 | Thermal... |
λ | 0.11 | W/m×K | 311.97 | Thermal... |
λ | 0.11 | W/m×K | 312.34 | Thermal... |
λ | 0.10 | W/m×K | 321.52 | Thermal... |
λ | 0.10 | W/m×K | 321.98 | Thermal... |
λ | 0.10 | W/m×K | 322.34 | Thermal... |
λ | 0.10 | W/m×K | 322.34 | Thermal... |
λ | 0.10 | W/m×K | 332.24 | Thermal... |
λ | 0.10 | W/m×K | 332.69 | Thermal... |
λ | 0.10 | W/m×K | 333.09 | Thermal... |
λ | 0.10 | W/m×K | 343.42 | Thermal... |
λ | 0.10 | W/m×K | 343.89 | Thermal... |
λ | 0.10 | W/m×K | 344.28 | Thermal... |
λ | 0.10 | W/m×K | 344.30 | Thermal... |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.67] | kPa | [264.32; 390.12] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.43045e+01 | |||
Coefficient B | -3.15633e+03 | |||
Coefficient C | -3.91420e+01 | |||
Temperature range, min. | 264.32 | |||
Temperature range, max. | 390.12 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 300 350 | ||||
Pvap | 1.33 | kPa | 264.32 | Calculated Property |
Pvap | 3.02 | kPa | 278.30 | Calculated Property |
Pvap | 6.27 | kPa | 292.28 | Calculated Property |
Pvap | 12.04 | kPa | 306.25 | Calculated Property |
Pvap | 21.66 | kPa | 320.23 | Calculated Property |
Pvap | 36.87 | kPa | 334.21 | Calculated Property |
Pvap | 59.82 | kPa | 348.19 | Calculated Property |
Pvap | 93.06 | kPa | 362.16 | Calculated Property |
Pvap | 139.57 | kPa | 376.14 | Calculated Property |
Pvap | 202.67 | kPa | 390.12 | Calculated Property |
Pvap | [1.78e-06; 2795.09] | kPa | [153.75; 535.25] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 7.98000e+01 | |||
Coefficient B | -6.76864e+03 | |||
Coefficient C | -9.76975e+00 | |||
Coefficient D | 7.54692e-06 | |||
Temperature range, min. | 153.75 | |||
Temperature range, max. | 535.25 | |||
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 2500 3000 200 300 400 500 | ||||
Pvap | 1.78e-06 | kPa | 153.75 | Calculated Property |
Pvap | 2.50e-03 | kPa | 196.14 | Calculated Property |
Pvap | 0.20 | kPa | 238.53 | Calculated Property |
Pvap | 3.38 | kPa | 280.92 | Calculated Property |
Pvap | 24.47 | kPa | 323.31 | Calculated Property |
Pvap | 103.66 | kPa | 365.69 | Calculated Property |
Pvap | 311.00 | kPa | 408.08 | Calculated Property |
Pvap | 742.27 | kPa | 450.47 | Calculated Property |
Pvap | 1518.05 | kPa | 492.86 | Calculated Property |
Pvap | 2795.09 | kPa | 535.25 | Calculated Property |
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