Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -4799.60 ± 1.70 | kJ/mol | NIST |
ΔfG° | -251.70 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -559.50 ± 2.10 | kJ/mol | NIST |
ΔfH°liquid | -635.10 ± 2.00 | kJ/mol | NIST |
ΔfusH° | 18.64 | kJ/mol | Joback Calculated Property |
ΔvapH° | [75.60; 76.30] | kJ/mol |
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ΔvapH° | 76.30 ± 0.90 | kJ/mol | NIST |
ΔvapH° | 75.60 ± 0.42 | kJ/mol | NIST |
ΔvapH° | 75.60 ± 0.50 | kJ/mol | NIST |
log10WS | -2.03 | Crippen Calculated Property | |
logPoct/wat | 2.287 | Crippen Calculated Property | |
McVol | 131.020 | ml/mol | McGowan Calculated Property |
Pc | [2778.00; 2780.00] | kPa |
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Pc | 2780.00 ± 300.00 | kPa | NIST |
Pc | 2778.00 ± 40.00 | kPa | NIST |
ρc | [260.01; 272.56] | kg/m3 |
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ρc | 260.01 ± 14.42 | kg/m3 | NIST |
ρc | 272.56 ± 5.77 | kg/m3 | NIST |
Inp | [180.80; 1161.00] |
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|
Inp | 1085.19 | NIST | |
Inp | 1116.70 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1161.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1124.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1140.00 | NIST | |
Inp | 1122.00 | NIST | |
Inp | 1108.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1114.00 | NIST | |
Inp | 1105.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1139.00 | NIST | |
Inp | 1123.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1130.00 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1104.00 | NIST | |
Inp | 1122.00 | NIST | |
Inp | 1097.00 | NIST | |
Inp | 1128.00 | NIST | |
Inp | 1126.00 | NIST | |
Inp | 1117.00 | NIST | |
Inp | Outlier 180.80 | NIST | |
Inp | Outlier 180.80 | NIST | |
Inp | 1128.00 | NIST | |
I | [1910.00; 1974.00] |
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|
I | 1962.50 | NIST | |
I | Outlier 1914.00 | NIST | |
I | 1969.00 | NIST | |
I | 1950.00 | NIST | |
I | 1965.00 | NIST | |
I | 1965.00 | NIST | |
I | 1968.00 | NIST | |
I | 1968.00 | NIST | |
I | Outlier 1910.00 | NIST | |
I | 1934.00 | NIST | |
I | 1960.00 | NIST | |
I | 1968.00 | NIST | |
I | 1968.00 | NIST | |
I | 1965.00 | NIST | |
I | 1937.00 | NIST | |
I | 1933.00 | NIST | |
I | 1928.00 | NIST | |
I | 1954.00 | NIST | |
I | 1918.00 | NIST | |
I | 1969.00 | NIST | |
I | 1974.00 | NIST | |
I | 1960.00 | NIST | |
I | 1946.00 | NIST | |
I | 1967.00 | NIST | |
I | 1962.50 | NIST | |
I | 1969.00 | NIST | |
Tboil | [500.15; 501.20] | K |
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Tboil | 501.20 | K | NIST |
Tboil | 500.15 | K | NIST |
Tc | [673.60; 675.00] | K |
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Tc | 675.00 ± 5.00 | K | NIST |
Tc | 673.60 ± 1.20 | K | NIST |
Tc | 674.60 ± 0.80 | K | NIST |
Tfus | 154.75 | K | NIST |
Vc | 0.502 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [309.75; 369.66] | J/mol×K | [528.05; 700.14] | ![]() |
T(K) Ideal gas heat capacity (J/mol×K) 310 320 330 340 350 360 370 550 600 650 700 | ||||
Cp,gas | 309.75 | J/mol×K | 528.05 | Joback Calculated Property |
Cp,gas | 320.87 | J/mol×K | 556.73 | Joback Calculated Property |
Cp,gas | 331.52 | J/mol×K | 585.41 | Joback Calculated Property |
Cp,gas | 341.71 | J/mol×K | 614.10 | Joback Calculated Property |
Cp,gas | 351.46 | J/mol×K | 642.78 | Joback Calculated Property |
Cp,gas | 360.77 | J/mol×K | 671.46 | Joback Calculated Property |
Cp,gas | 369.66 | J/mol×K | 700.14 | Joback Calculated Property |
η | [0.0001397; 0.0284980] | Pa×s | [275.67; 528.05] | ![]() |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-3 0.01 0.02 0.02 0.03 0.03 300 400 500 | ||||
η | 0.0284980 | Pa×s | 275.67 | Joback Calculated Property |
η | 0.0065326 | Pa×s | 317.73 | Joback Calculated Property |
η | 0.0021132 | Pa×s | 359.80 | Joback Calculated Property |
η | 0.0008658 | Pa×s | 401.86 | Joback Calculated Property |
η | 0.0004201 | Pa×s | 443.92 | Joback Calculated Property |
η | 0.0002310 | Pa×s | 485.99 | Joback Calculated Property |
η | 0.0001397 | Pa×s | 528.05 | Joback Calculated Property |
ΔvapH | 61.80 | kJ/mol | 451.50 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.33; 202.65] | kPa | [386.55; 528.29] |
The Yaw...
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Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.58601e+01 | |||
Coefficient B | -4.63462e+03 | |||
Coefficient C | -8.89300e+01 | |||
Temperature range, min. | 386.55 | |||
Temperature range, max. | 528.29 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 | ||||
Pvap | 1.33 | kPa | 386.55 | Calculated Property |
Pvap | 2.92 | kPa | 402.30 | Calculated Property |
Pvap | 5.92 | kPa | 418.05 | Calculated Property |
Pvap | 11.26 | kPa | 433.80 | Calculated Property |
Pvap | 20.25 | kPa | 449.55 | Calculated Property |
Pvap | 34.67 | kPa | 465.29 | Calculated Property |
Pvap | 56.85 | kPa | 481.04 | Calculated Property |
Pvap | 89.73 | kPa | 496.79 | Calculated Property |
Pvap | 136.91 | kPa | 512.54 | Calculated Property |
Pvap | 202.65 | kPa | 528.29 | Calculated Property |
Find more compounds similar to Hexanoic acid, 2-ethyl-.
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