Property | Value | Unit | Source |
---|---|---|---|
ΔfG° | 201.72 | kJ/mol | Joback Calculated Property |
ΔfH°gas | -662.53 | kJ/mol | Joback Calculated Property |
ΔfusH° | 73.46 | kJ/mol | Joback Calculated Property |
ΔvapH° | [152.30; 164.50] | kJ/mol | |
ΔvapH° | 152.30 | kJ/mol | NIST |
ΔvapH° | 164.50 ± 0.40 | kJ/mol | NIST |
log10WS | -12.38 | Crippen Calculated Property | |
logPoct/wat | 11.949 | Crippen Calculated Property | |
McVol | 433.560 | ml/mol | McGowan Calculated Property |
Pc | 595.46 | kPa | Joback Calculated Property |
Inp | [467.01; 488.40] | ||
Inp | 467.01 | NIST | |
Inp | 488.40 | NIST | |
Tboil | 722.90 | K | NIST |
Tc | 850.00 | K | Critica... |
Tfus | [338.50; 344.00] | K | |
Tfus | 338.70 ± 0.30 | K | NIST |
Tfus | 338.60 ± 0.40 | K | NIST |
Tfus | 338.53 ± 0.25 | K | NIST |
Tfus | 339.40 ± 2.00 | K | NIST |
Tfus | 339.00 ± 2.00 | K | NIST |
Tfus | 339.00 ± 0.10 | K | NIST |
Tfus | 338.90 ± 0.60 | K | NIST |
Tfus | 338.70 ± 1.00 | K | NIST |
Tfus | 338.70 ± 1.00 | K | NIST |
Tfus | Outlier 344.00 ± 1.50 | K | NIST |
Tfus | 338.90 ± 3.00 | K | NIST |
Tfus | 338.70 ± 0.30 | K | NIST |
Tfus | 338.90 ± 0.80 | K | NIST |
Tfus | 339.00 ± 2.00 | K | NIST |
Tfus | 339.00 ± 2.00 | K | NIST |
Tfus | 340.00 ± 2.00 | K | NIST |
Tfus | 339.00 ± 2.00 | K | NIST |
Tfus | 339.00 ± 2.00 | K | NIST |
Tfus | Outlier 343.00 ± 2.00 | K | NIST |
Tfus | 338.50 ± 0.80 | K | NIST |
Tfus | 338.80 ± 1.00 | K | NIST |
Tfus | 339.30 ± 1.00 | K | NIST |
Ttriple | 334.20 | K | Thermal... |
Vc | 1.716 | m3/kmol | Joback Calculated Property |
Property | Value | Unit | Temperature (K) | Source |
---|---|---|---|---|
Cp,gas | [1482.03; 1624.56] | J/mol×K | [885.80; 1091.97] | |
T(K) Ideal gas heat capacity (J/mol×K) 1480 1500 1520 1540 1560 1580 1600 1620 900 950 1000 1050 | ||||
Cp,gas | 1482.03 | J/mol×K | 885.80 | Joback Calculated Property |
Cp,gas | 1509.37 | J/mol×K | 920.16 | Joback Calculated Property |
Cp,gas | 1535.15 | J/mol×K | 954.52 | Joback Calculated Property |
Cp,gas | 1559.49 | J/mol×K | 988.88 | Joback Calculated Property |
Cp,gas | 1582.44 | J/mol×K | 1023.25 | Joback Calculated Property |
Cp,gas | 1604.10 | J/mol×K | 1057.61 | Joback Calculated Property |
Cp,gas | 1624.56 | J/mol×K | 1091.97 | Joback Calculated Property |
Cp,solid | [558.00; 808.80] | J/mol×K | [300.00; 301.00] | |
Cp,solid | 558.00 | J/mol×K | 300.00 | NIST |
Cp,solid | 808.80 | J/mol×K | 301.00 | NIST |
η | [0.0000243; 0.0010730] | Pa×s | [427.86; 885.80] | |
T(K) Dynamic viscosity (Pa×s) 0 2.00e-4 4.00e-4 6.00e-4 8.00e-4 1.00e-3 500 600 700 800 | ||||
η | 0.0010730 | Pa×s | 427.86 | Joback Calculated Property |
η | 0.0003539 | Pa×s | 504.18 | Joback Calculated Property |
η | 0.0001562 | Pa×s | 580.51 | Joback Calculated Property |
η | 0.0000834 | Pa×s | 656.83 | Joback Calculated Property |
η | 0.0000507 | Pa×s | 733.15 | Joback Calculated Property |
η | 0.0000339 | Pa×s | 809.48 | Joback Calculated Property |
η | 0.0000243 | Pa×s | 885.80 | Joback Calculated Property |
ΔfusH | [37.49; 68.83] | kJ/mol | [335.30; 338.70] | |
ΔfusH | 37.49 | kJ/mol | 335.30 | NIST |
ΔfusH | 68.83 | kJ/mol | 338.70 | NIST |
ΔfusH | 68.83 | kJ/mol | 338.70 | NIST |
ΔvapH | [111.30; 152.30] | kJ/mol | [298.15; 609.00] | |
ΔvapH | 152.30 | kJ/mol | 298.15 | Vapor P... |
ΔvapH | 143.00 ± 2.00 | kJ/mol | 454.50 | NIST |
ΔvapH | 111.30 | kJ/mol | 609.00 | NIST |
Pvap | [1.13e-03; 414.10] | kPa | [432.36; 809.60] | |
T(K) Vapor pressure (kPa) 0 100 200 300 400 500 600 700 800 | ||||
Pvap | 1.15e-03 | kPa | 432.36 | Experim... |
Pvap | 1.13e-03 | kPa | 432.37 | Experim... |
Pvap | 2.33e-03 | kPa | 442.48 | Experim... |
Pvap | 4.57e-03 | kPa | 452.32 | Experim... |
Pvap | 4.51e-03 | kPa | 452.34 | Experim... |
Pvap | 82.32 | kPa | 713.50 | Critica... |
Pvap | 127.80 | kPa | 737.80 | Critica... |
Pvap | 190.20 | kPa | 761.20 | Critica... |
Pvap | 282.40 | kPa | 786.00 | Critica... |
Pvap | 414.10 | kPa | 809.60 | Critica... |
ΔfusS | [111.82; 203.24] | J/mol×K | [335.30; 338.70] | |
ΔfusS | 111.82 | J/mol×K | 335.30 | NIST |
ΔfusS | 203.24 | J/mol×K | 338.70 | NIST |
Property | Value | Unit | Pressure (kPa) | Source |
---|---|---|---|---|
Tboilr | 531.70 | K | 0.40 | NIST |
Find more compounds similar to Triacontane.
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.