Property | Value | Unit | Source |
---|---|---|---|
ω | 0.3300 | KDB | |
AP | 340.350 | K | KDB |
ΔcH°liquid | -5471.00 ± 1.40 | kJ/mol | NIST |
ΔfG° | 21.27 | kJ/mol | KDB |
Δc,grossH | 5470.91 | kJ/mol | KDB |
Δc,netH | 5074.774 | kJ/mol | KDB |
ΔfH°gas | [-211.30; -211.20] | kJ/mol | |
ΔfH°gas | -211.30 | kJ/mol | KDB |
ΔfH°gas | -211.20 ± 1.30 | kJ/mol | NIST |
ΔfH°liquid | -249.70 ± 1.30 | kJ/mol | NIST |
ΔfusH° | 9.43 | kJ/mol | Joback Calculated Property |
ΔvapH° | [38.50; 38.56] | kJ/mol | |
ΔvapH° | 38.56 | kJ/mol | NIST |
ΔvapH° | 38.50 | kJ/mol | NIST |
ΔvapH° | 38.50 ± 0.10 | kJ/mol | NIST |
ΔvapH° | 38.52 | kJ/mol | NIST |
log10WS | -2.69 | Crippen Calculated Property | |
logPoct/wat | 3.079 | Crippen Calculated Property | |
McVol | 123.580 | ml/mol | McGowan Calculated Property |
Pc | [2700.00; 2700.40] | kPa | |
Pc | 2700.00 | kPa | KDB |
Pc | 2700.00 ± 40.00 | kPa | NIST |
Pc | 2700.40 ± 40.53 | kPa | NIST |
ρc | [258.16; 258.16] | kg/m3 | |
ρc | 258.16 ± 4.57 | kg/m3 | NIST |
ρc | 258.16 ± 4.57 | kg/m3 | NIST |
Inp | [743.00; 767.00] | ||
Inp | 762.00 | NIST | |
Inp | Outlier 743.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 765.50 | NIST | |
Inp | 758.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 760.30 | NIST | |
Inp | 762.75 | NIST | |
Inp | 760.20 | NIST | |
Inp | 761.50 | NIST | |
Inp | 762.70 | NIST | |
Inp | 763.80 | NIST | |
Inp | 758.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 763.20 | NIST | |
Inp | 763.30 | NIST | |
Inp | 761.10 | NIST | |
Inp | 763.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 761.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 756.00 | NIST | |
Inp | 758.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 761.50 | NIST | |
Inp | 763.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 758.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 758.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 762.40 | NIST | |
Inp | 755.95 | NIST | |
Inp | 760.40 | NIST | |
Inp | 759.70 | NIST | |
Inp | 757.28 | NIST | |
Inp | 758.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 761.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 767.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 756.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 760.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 762.00 | NIST | |
Inp | 763.00 | NIST | |
Inp | 762.75 | NIST | |
Inp | 758.00 | NIST | |
Inp | 765.00 | NIST | |
Inp | 764.00 | NIST | |
Inp | 755.00 | NIST | |
Inp | 759.00 | NIST | |
Inp | 762.40 | NIST | |
Tboil | [387.15; 388.90] | K | |
Tboil | 388.81 | K | KDB |
Tboil | 388.80 | K | NIST |
Tboil | 388.80 | K | NIST |
Tboil | 388.80 ± 0.20 | K | NIST |
Tboil | 388.70 ± 0.10 | K | NIST |
Tboil | 388.55 ± 0.20 | K | NIST |
Tboil | 388.65 ± 0.30 | K | NIST |
Tboil | 388.90 ± 0.15 | K | NIST |
Tboil | 388.80 ± 0.05 | K | NIST |
Tboil | 388.70 ± 0.30 | K | NIST |
Tboil | 388.80 ± 0.02 | K | NIST |
Tboil | 388.85 ± 0.10 | K | NIST |
Tboil | 388.85 ± 0.20 | K | NIST |
Tboil | 388.80 ± 0.05 | K | NIST |
Tboil | 388.85 ± 0.40 | K | NIST |
Tboil | Outlier 387.15 ± 1.50 | K | NIST |
Tc | [567.00; 567.10] | K | |
Tc | 567.10 | K | KDB |
Tc | 567.10 ± 0.50 | K | NIST |
Tc | 567.00 | K | NIST |
Tc | 567.02 ± 0.40 | K | NIST |
Tfus | [157.97; 158.65] | K | |
Tfus | 158.20 | K | KDB |
Tfus | 157.97 ± 0.20 | K | NIST |
Tfus | 158.21 ± 0.10 | K | NIST |
Tfus | 157.97 ± 0.20 | K | NIST |
Tfus | 157.97 ± 0.20 | K | NIST |
Tfus | 158.10 ± 0.02 | K | NIST |
Tfus | 158.14 ± 0.06 | K | NIST |
Tfus | 158.14 ± 0.05 | K | NIST |
Tfus | 158.15 ± 0.20 | K | NIST |
Tfus | Outlier 158.65 ± 0.50 | K | NIST |
Vc | [0.442; 0.442] | m3/kmol | |
Vc | 0.442 | m3/kmol | KDB |
Vc | 0.442 | m3/kmol | NIST |
Zc | 0.2530990 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [243.09; 299.57] | J/mol×K | [399.70; 522.20] | |
Cp,gas | 243.09 | J/mol×K | 399.70 | NIST |
Cp,gas | 272.80 | J/mol×K | 461.90 | NIST |
Cp,gas | 299.57 | J/mol×K | 522.20 | NIST |
η | [0.0002299; 0.0231912] | Pa×s | [149.92; 381.56] | |
η | 0.0231912 | Pa×s | 149.92 | Joback Calculated Property |
η | 0.0048914 | Pa×s | 188.53 | Joback Calculated Property |
η | 0.0017511 | Pa×s | 227.13 | Joback Calculated Property |
η | 0.0008449 | Pa×s | 265.74 | Joback Calculated Property |
η | 0.0004905 | Pa×s | 304.35 | Joback Calculated Property |
η | 0.0003218 | Pa×s | 342.95 | Joback Calculated Property |
η | 0.0002299 | Pa×s | 381.56 | Joback Calculated Property |
ΔvapH | [32.93; 37.40] | kJ/mol | [350.50; 388.80] | |
ΔvapH | 37.40 | kJ/mol | 350.50 | NIST |
ΔvapH | 32.93 | kJ/mol | 388.80 | NIST |
n0 | 1.40167 | 298.15 | KDB | |
ρl | 719.00 | kg/m3 | 293.00 | KDB |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [283.28; 415.34] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.41006e+01 | |||
Coefficient B | -3.19130e+03 | |||
Coefficient C | -5.22440e+01 | |||
Temperature range, min. | 283.28 | |||
Temperature range, max. | 415.34 | |||
Pvap | 1.33 | kPa | 283.28 | Calculated Property |
Pvap | 3.04 | kPa | 297.95 | Calculated Property |
Pvap | 6.32 | kPa | 312.63 | Calculated Property |
Pvap | 12.16 | kPa | 327.30 | Calculated Property |
Pvap | 21.88 | kPa | 341.97 | Calculated Property |
Pvap | 37.22 | kPa | 356.65 | Calculated Property |
Pvap | 60.27 | kPa | 371.32 | Calculated Property |
Pvap | 93.56 | kPa | 385.99 | Calculated Property |
Pvap | 139.95 | kPa | 400.67 | Calculated Property |
Pvap | 202.64 | kPa | 415.34 | Calculated Property |
Pvap | [0.14; 2694.23] | kPa | [250.00; 567.00] | KDB Vap... |
Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
Coefficient A | 8.38476e+01 | |||
Coefficient B | -7.34958e+03 | |||
Coefficient C | -1.02987e+01 | |||
Coefficient D | 7.18885e-06 | |||
Temperature range, min. | 250.00 | |||
Temperature range, max. | 567.00 | |||
Pvap | 0.14 | kPa | 250.00 | Calculated Property |
Pvap | 1.56 | kPa | 285.22 | Calculated Property |
Pvap | 9.30 | kPa | 320.44 | Calculated Property |
Pvap | 36.53 | kPa | 355.67 | Calculated Property |
Pvap | 107.41 | kPa | 390.89 | Calculated Property |
Pvap | 257.01 | kPa | 426.11 | Calculated Property |
Pvap | 529.94 | kPa | 461.33 | Calculated Property |
Pvap | 980.08 | kPa | 496.56 | Calculated Property |
Pvap | 1673.37 | kPa | 531.78 | Calculated Property |
Pvap | 2694.23 | kPa | 567.00 | Calculated Property |
Find more compounds similar to Pentane, 3-ethyl-2-methyl-.
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