Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | -175.34 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -634.00 ± 2.00 | kJ/mol | NIST |
ΔfH°liquid | -705.40 ± 1.20 | kJ/mol | NIST |
ΔfusH° | 36.10 | kJ/mol | Thermal... |
ΔvapH° | [71.40; 72.00] | kJ/mol | |
ΔvapH° | 72.00 ± 1.00 | kJ/mol | NIST |
ΔvapH° | 71.40 | kJ/mol | NIST |
log10WS | -4.13 | Crippen Calculated Property | |
logPoct/wat | 4.080 | Crippen Calculated Property | |
McVol | 201.470 | ml/mol | McGowan Calculated Property |
Pc | 1707.53 | kPa | Joback Calculated Property |
Inp | [1475.00; 1498.00] | ||
Inp | 1476.00 | NIST | |
Inp | 1477.00 | NIST | |
Inp | 1478.00 | NIST | |
Inp | 1479.00 | NIST | |
Inp | 1493.00 | NIST | |
Inp | 1482.00 | NIST | |
Inp | 1491.00 | NIST | |
Inp | 1498.00 | NIST | |
Inp | 1483.00 | NIST | |
Inp | 1495.40 | NIST | |
Inp | 1494.00 | NIST | |
Inp | 1496.00 | NIST | |
Inp | 1477.00 | NIST | |
Inp | 1479.00 | NIST | |
Inp | 1475.00 | NIST | |
Inp | 1491.00 | NIST | |
Inp | 1496.00 | NIST | |
Inp | 1494.00 | NIST | |
Inp | 1498.00 | NIST | |
Inp | 1493.00 | NIST | |
Inp | 1479.00 | NIST | |
Inp | 1479.00 | NIST | |
Inp | 1491.00 | NIST | |
Inp | 1494.00 | NIST | |
Inp | 1495.40 | NIST | |
Inp | 1479.00 | NIST | |
I | [1725.00; 1775.00] | ||
I | 1744.00 | NIST | |
I | 1763.00 | NIST | |
I | 1739.00 | NIST | |
I | 1775.00 | NIST | |
I | 1740.00 | NIST | |
I | 1757.00 | NIST | |
I | 1774.00 | NIST | |
I | 1737.00 | NIST | |
I | 1754.00 | NIST | |
I | 1732.00 | NIST | |
I | 1725.00 | NIST | |
I | 1737.00 | NIST | |
I | 1732.00 | NIST | |
I | 1739.00 | NIST | |
I | 1725.00 | NIST | |
I | 1725.00 | NIST | |
Tboil | 573.13 | K | Joback Calculated Property |
Tc | 741.92 | K | Joback Calculated Property |
Tfus | 308.43 | K | Joback Calculated Property |
Vc | 0.787 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [514.80; 603.14] | J/mol×K | [573.13; 741.92] | |
Cp,gas | 514.80 | J/mol×K | 573.13 | Joback Calculated Property |
Cp,gas | 531.11 | J/mol×K | 601.26 | Joback Calculated Property |
Cp,gas | 546.77 | J/mol×K | 629.39 | Joback Calculated Property |
Cp,gas | 561.79 | J/mol×K | 657.52 | Joback Calculated Property |
Cp,gas | 576.19 | J/mol×K | 685.66 | Joback Calculated Property |
Cp,gas | 589.97 | J/mol×K | 713.79 | Joback Calculated Property |
Cp,gas | 603.14 | J/mol×K | 741.92 | Joback Calculated Property |
η | [0.0001702; 0.0029408] | Pa×s | [308.43; 573.13] | |
η | 0.0029408 | Pa×s | 308.43 | Joback Calculated Property |
η | 0.0013589 | Pa×s | 352.55 | Joback Calculated Property |
η | 0.0007456 | Pa×s | 396.66 | Joback Calculated Property |
η | 0.0004613 | Pa×s | 440.78 | Joback Calculated Property |
η | 0.0003115 | Pa×s | 484.90 | Joback Calculated Property |
η | 0.0002245 | Pa×s | 529.01 | Joback Calculated Property |
η | 0.0001702 | Pa×s | 573.13 | Joback Calculated Property |
ΔfusH | 36.16 | kJ/mol | 259.20 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 378.20 | K | 0.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.64] | kPa | [410.00; 555.04] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.63515e+01 | |||
Coefficient B | -5.12005e+03 | |||
Coefficient C | -9.12700e+01 | |||
Temperature range, min. | 410.00 | |||
Temperature range, max. | 555.04 | |||
Pvap | 1.33 | kPa | 410.00 | Calculated Property |
Pvap | 2.89 | kPa | 426.12 | Calculated Property |
Pvap | 5.83 | kPa | 442.23 | Calculated Property |
Pvap | 11.06 | kPa | 458.35 | Calculated Property |
Pvap | 19.88 | kPa | 474.46 | Calculated Property |
Pvap | 34.10 | kPa | 490.58 | Calculated Property |
Pvap | 56.07 | kPa | 506.69 | Calculated Property |
Pvap | 88.84 | kPa | 522.81 | Calculated Property |
Pvap | 136.18 | kPa | 538.92 | Calculated Property |
Pvap | 202.64 | kPa | 555.04 | Calculated Property |
Find more compounds similar to Undecanoic acid, ethyl ester.
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