Property | Value | Unit | Source |
---|---|---|---|
ΔcH°liquid | -11160.70 | kJ/mol | NIST |
ΔfG° | -84.84 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -562.44 | kJ/mol | Joback Calculated Property |
ΔfH°liquid | -764.80 | kJ/mol | NIST |
ΔfusH° | 48.26 | kJ/mol | Joback Calculated Property |
ΔvapH° | 79.05 | kJ/mol | Joback Calculated Property |
log10WS | -6.31 | Crippen Calculated Property | |
logPoct/wat | 6.109 | Crippen Calculated Property | |
McVol | 267.620 | ml/mol | McGowan Calculated Property |
Pc | 1332.96 | kPa | Joback Calculated Property |
Inp | [2090.00; 2180.00] | ||
Inp | 2140.00 | NIST | |
Inp | 2171.00 | NIST | |
Inp | 2115.00 | NIST | |
Inp | 2097.00 | NIST | |
Inp | 2102.00 | NIST | |
Inp | 2175.00 | NIST | |
Inp | 2141.00 | NIST | |
Inp | 2137.00 | NIST | |
Inp | 2152.00 | NIST | |
Inp | 2141.00 | NIST | |
Inp | 2147.00 | NIST | |
Inp | 2152.00 | NIST | |
Inp | 2113.00 | NIST | |
Inp | 2146.10 | NIST | |
Inp | 2130.00 | NIST | |
Inp | 2175.00 | NIST | |
Inp | 2175.00 | NIST | |
Inp | 2131.00 | NIST | |
Inp | 2141.00 | NIST | |
Inp | 2147.00 | NIST | |
Inp | 2147.00 | NIST | |
Inp | 2116.00 | NIST | |
Inp | 2146.00 | NIST | |
Inp | Outlier 2090.00 | NIST | |
Inp | 2180.00 | NIST | |
Inp | 2180.00 | NIST | |
Inp | 2115.00 | NIST | |
Inp | 2115.00 | NIST | |
Inp | 2110.00 | NIST | |
Inp | 2161.00 | NIST | |
Inp | 2112.00 | NIST | |
Inp | 2115.00 | NIST | |
Inp | 2131.00 | NIST | |
Inp | 2152.00 | NIST | |
Inp | 2175.00 | NIST | |
Inp | 2120.00 | NIST | |
Inp | 2173.00 | NIST | |
Inp | 2161.00 | NIST | |
Inp | 2098.00 | NIST | |
Inp | 2112.00 | NIST | |
Inp | 2146.00 | NIST | |
Inp | 2141.00 | NIST | |
Inp | 2155.00 | NIST | |
Inp | 2140.00 | NIST | |
Inp | 2131.00 | NIST | |
Inp | 2161.00 | NIST | |
Inp | 2155.00 | NIST | |
I | [3142.00; 3200.00] | ||
I | 3184.00 | NIST | |
I | 3173.00 | NIST | |
I | 3172.00 | NIST | |
I | 3142.00 | NIST | |
I | 3150.00 | NIST | |
I | 3157.00 | NIST | |
I | 3157.00 | NIST | |
I | 3184.00 | NIST | |
I | 3200.00 | NIST | |
I | 3172.00 | NIST | |
I | 3157.00 | NIST | |
Tboil | 761.45 | K | Joback Calculated Property |
Tc | 937.21 | K | Joback Calculated Property |
Tfus | [286.70; 289.45] | K | |
Tfus | 286.70 | K | Solid-L... |
Tfus | 289.45 ± 0.30 | K | NIST |
Tfus | 289.45 ± 0.50 | K | NIST |
Vc | 1.048 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [811.35; 899.26] | J/mol×K | [761.45; 937.21] | |
T(K) Ideal gas heat capacity (J/mol×K) 820 840 860 880 900 800 850 900 | ||||
Cp,gas | 811.35 | J/mol×K | 761.45 | Joback Calculated Property |
Cp,gas | 827.83 | J/mol×K | 790.74 | Joback Calculated Property |
Cp,gas | 843.52 | J/mol×K | 820.04 | Joback Calculated Property |
Cp,gas | 858.48 | J/mol×K | 849.33 | Joback Calculated Property |
Cp,gas | 872.72 | J/mol×K | 878.62 | Joback Calculated Property |
Cp,gas | 886.31 | J/mol×K | 907.92 | Joback Calculated Property |
Cp,gas | 899.26 | J/mol×K | 937.21 | Joback Calculated Property |
η | [0.0000210; 0.0023727] | Pa×s | [398.29; 761.45] | |
T(K) Dynamic viscosity (Pa×s) 0 5.00e-4 1.00e-3 1.50e-3 2.00e-3 2.50e-3 400 500 600 700 | ||||
η | 0.0023727 | Pa×s | 398.29 | Joback Calculated Property |
η | 0.0006419 | Pa×s | 458.82 | Joback Calculated Property |
η | 0.0002355 | Pa×s | 519.34 | Joback Calculated Property |
η | 0.0001065 | Pa×s | 579.87 | Joback Calculated Property |
η | 0.0000560 | Pa×s | 640.40 | Joback Calculated Property |
η | 0.0000329 | Pa×s | 700.92 | Joback Calculated Property |
η | 0.0000210 | Pa×s | 761.45 | Joback Calculated Property |
ΔfusH | [39.60; 39.60] | kJ/mol | [286.50; 286.50] | |
ΔfusH | 39.60 | kJ/mol | 286.50 | NIST |
ΔfusH | 39.60 | kJ/mol | 286.50 | NIST |
ΔvapH | [83.80; 132.60] | kJ/mol | [298.15; 537.00] | |
ΔvapH | 132.60 | kJ/mol | 298.15 | Vaporiz... |
ΔvapH | 83.80 | kJ/mol | 537.00 | NIST |
Pvap | [1.33; 9.33] | kPa | [496.70; 547.40] | |
T(K) Vapor pressure (kPa) 2 4 6 8 10 500 520 540 | ||||
Pvap | 1.33 | kPa | 496.70 | Vapor p... |
Pvap | 2.67 | kPa | 513.10 | Vapor p... |
Pvap | 4.00 | kPa | 524.70 | Vapor p... |
Pvap | 5.33 | kPa | 532.10 | Vapor p... |
Pvap | 6.67 | kPa | 538.80 | Vapor p... |
Pvap | 8.00 | kPa | 543.80 | Vapor p... |
Pvap | 9.33 | kPa | 547.40 | Vapor p... |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 467.70 | K | 0.10 | NIST |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Pvap | [1.36; 203.46] | kPa | [514.15; 709.15] | The Yaw... |
Equation | ln(Pvp) = A + B/(T + C) | |||
Coefficient A | 1.52924e+01 | |||
Coefficient B | -5.81882e+03 | |||
Coefficient C | -1.25923e+02 | |||
Temperature range, min. | 514.15 | |||
Temperature range, max. | 709.15 | |||
T(K) Vapor pressure (kPa) 0 50 100 150 200 550 600 650 700 | ||||
Pvap | 1.36 | kPa | 514.15 | Calculated Property |
Pvap | 2.99 | kPa | 535.82 | Calculated Property |
Pvap | 6.11 | kPa | 557.48 | Calculated Property |
Pvap | 11.63 | kPa | 579.15 | Calculated Property |
Pvap | 20.90 | kPa | 600.82 | Calculated Property |
Pvap | 35.66 | kPa | 622.48 | Calculated Property |
Pvap | 58.21 | kPa | 644.15 | Calculated Property |
Pvap | 91.35 | kPa | 665.82 | Calculated Property |
Pvap | 138.45 | kPa | 687.48 | Calculated Property |
Pvap | 203.46 | kPa | 709.15 | Calculated Property |
Find more compounds similar to Oleic Acid.
Find more mixtures with Oleic Acid.
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.