- InChI
- InChI=1S/C24H50/c1-3-5-7-9-11-13-15-17-19-21-23-24-22-20-18-16-14-12-10-8-6-4-2/h3-24H2,1-2H3
- InChI Key
- POOSGDOYLQNASK-UHFFFAOYSA-N
- Formula
- C24H50
- SMILES
- CCCCCCCCCCCCCCCCCCCCCCCC
- Molecular Weight1
- 338.65
- CAS
- 646-31-1
- Other Names
-
- n-Tetracosane
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔsubH° : Enthalpy of sublimation at standard conditions (kJ/mol).
- ΔsubH : Enthalpy of sublimation at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- Pc : Critical Pressure (kPa).
- Psub : Sublimation pressure (kPa).
- Pvap : Vapor pressure (kPa).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- γ : Surface Tension (N/m).
- S°solid,1 bar : Solid phase molar entropy at standard conditions (J/mol×K).
- Tboil : Normal Boiling Point Temperature (K).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ΔfG° | 151.20 | kJ/mol | Joback Calculated Property |
| ΔfH°gas | -538.69 | kJ/mol | Joback Calculated Property |
| ΔfusH° | 57.92 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 162.00 ± 12.00 | kJ/mol | NIST |
| ΔvapH° | [121.90; 126.80] | kJ/mol |
|
| ΔvapH° | 121.90 | kJ/mol | NIST |
| ΔvapH° | 126.80 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 125.70 ± 1.60 | kJ/mol | NIST |
| ΔvapH° | 126.20 ± 2.30 | kJ/mol | NIST |
| log10WS | -9.87 | Crippen Calculated Property | |
| logPoct/wat | 9.608 | Crippen Calculated Property | |
| McVol | 349.020 | ml/mol | McGowan Calculated Property |
| Pc | [866.00; 900.00] | kPa |
|
| Pc | 870.00 | kPa | KDB |
| Pc | 900.00 ± 200.00 | kPa | NIST |
| Pc | 866.00 ± 40.00 | kPa | NIST |
| Inp | [366.00; 402.60] |
|
|
| Inp | 382.35 | NIST | |
| Inp | 389.39 | NIST | |
| Inp | 402.50 | NIST | |
| Inp | 402.60 | NIST | |
| Inp | 366.00 | NIST | |
| S°solid,1 bar | 651.00 | J/mol×K | NIST |
| Tboil | [516.00; 664.50] | K |
|
| Tboil | 664.50 | K | NIST |
| Tboil | 597.30 ± 4.00 | K | NIST |
| Tboil | 516.00 ± 6.00 | K | NIST |
| Tc | [799.80; 801.00] | K |
|
| Tc | 800.00 | K | KDB |
| Tc | 801.00 | K | Critica... |
| Tc | 800.00 ± 8.00 | K | NIST |
| Tc | 799.80 ± 3.00 | K | NIST |
| Tfus | [321.21; 324.10] | K |
|
| Tfus | 321.21 | K | Solid-l... |
| Tfus | 324.10 | K | Solid-l... |
| Ttriple | [320.80; 323.65] | K |
|
| Ttriple | 320.80 | K | Thermal... |
| Ttriple | 321.40 | K | Solubil... |
| Ttriple | 323.65 ± 1.00 | K | NIST |
| Vc | 1.379 | m3/kmol | Joback Calculated Property |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [1087.48; 1209.76] | J/mol×K | [748.52; 918.06] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 1080 1100 1120 1140 1160 1180 1200 1220 750 800 850 900 | ||||
| Cp,gas | 1087.48 | J/mol×K | 748.52 | Joback Calculated Property |
| Cp,gas | 1110.30 | J/mol×K | 776.78 | Joback Calculated Property |
| Cp,gas | 1132.09 | J/mol×K | 805.03 | Joback Calculated Property |
| Cp,gas | 1152.90 | J/mol×K | 833.29 | Joback Calculated Property |
| Cp,gas | 1172.75 | J/mol×K | 861.55 | Joback Calculated Property |
| Cp,gas | 1191.69 | J/mol×K | 889.81 | Joback Calculated Property |
| Cp,gas | 1209.76 | J/mol×K | 918.06 | Joback Calculated Property |
| Cp,liquid | [772.50; 805.00] | J/mol×K | [330.63; 353.00] |
|
| Cp,liquid | 772.50 | J/mol×K | 330.63 | NIST |
| Cp,liquid | 805.00 | J/mol×K | 353.00 | NIST |
| Cp,solid | [601.00; 730.90] | J/mol×K | [298.15; 300.00] |
|
| Cp,solid | 730.90 | J/mol×K | 298.15 | NIST |
| Cp,solid | 601.00 | J/mol×K | 300.00 | NIST |
| η | [0.0000578; 0.0023389] | Pa×s | [360.24; 748.52] |
|
|
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 | 0.0023389 | Pa×s | 360.24 | Joback Calculated Property |
| η | 0.0007891 | Pa×s | 424.95 | Joback Calculated Property |
| η | 0.0003548 | Pa×s | 489.67 | Joback Calculated Property |
| η | 0.0001923 | Pa×s | 554.38 | Joback Calculated Property |
| η | 0.0001184 | Pa×s | 619.09 | Joback Calculated Property |
| η | 0.0000799 | Pa×s | 683.81 | Joback Calculated Property |
| η | 0.0000578 | Pa×s | 748.52 | Joback Calculated Property |
| ΔfusH | [31.30; 81.75] | kJ/mol | [321.30; 324.10] |
|
|
T(K) Enthalpy of fusion at a given temperature (kJ/mol) 30 40 50 60 70 80 322 323 324 | ||||
| ΔfusH | 31.30 | kJ/mol | 321.30 | NIST |
| ΔfusH | 81.75 | kJ/mol | 322.00 | NIST |
| ΔfusH | 53.80 | kJ/mol | 323.40 | NIST |
| ΔfusH | 59.31 | kJ/mol | 324.10 | NIST |
| ΔfusH | 54.89 | kJ/mol | 324.10 | NIST |
| ΔfusH | 54.89 | kJ/mol | 324.10 | NIST |
| ΔsubH | 164.90 ± 1.80 | kJ/mol | 315.50 | NIST |
| ΔvapH | [86.20; 126.00] | kJ/mol | [298.00; 535.50] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 90 100 110 120 300 400 500 | ||||
| ΔvapH | 116.10 | kJ/mol | 298.00 | A Compa... |
| ΔvapH | 121.90 | kJ/mol | 298.15 | Vapor P... |
| ΔvapH | 105.10 ± 0.50 | kJ/mol | 353.00 | NIST |
| ΔvapH | 112.00 | kJ/mol | 393.00 | NIST |
| ΔvapH | 126.00 ± 2.00 | kJ/mol | 405.50 | NIST |
| ΔvapH | 111.20 | kJ/mol | 418.00 | NIST |
| ΔvapH | 95.20 | kJ/mol | 452.50 | NIST |
| ΔvapH | 86.20 ± 4.60 | kJ/mol | 474.00 | NIST |
| ΔvapH | 92.60 | kJ/mol | 520.50 | NIST |
| ΔvapH | 86.60 | kJ/mol | 535.50 | NIST |
| Psub | 1.23e-06 | kPa | 322.94 | Vapor a... |
| Pvap | [4.30e-06; 0.01] | kPa | [333.46; 417.75] |
|
|
T(K) Vapor pressure (kPa) 0 2.00e-3 4.00e-3 6.00e-3 8.00e-3 0.01 340 360 380 400 | ||||
| Pvap | 4.30e-06 | kPa | 333.46 | A Gas S... |
| Pvap | 4.35e-05 | kPa | 353.43 | A Gas S... |
| Pvap | 4.50e-05 | kPa | 353.97 | A Gas S... |
| Pvap | 3.07e-04 | kPa | 373.17 | A Gas S... |
| Pvap | 3.16e-04 | kPa | 373.61 | A Gas S... |
| Pvap | 5.24e-04 | kPa | 379.15 | A Gas S... |
| Pvap | 1.72e-03 | kPa | 393.20 | A Gas S... |
| Pvap | 1.72e-03 | kPa | 393.20 | A Gas S... |
| Pvap | 2.41e-03 | kPa | 397.55 | A Gas S... |
| Pvap | 8.43e-03 | kPa | 414.68 | A Gas S... |
| Pvap | 0.01 | kPa | 417.75 | A Gas S... |
| ΔfusS | [97.42; 253.90] | J/mol×K | [321.30; 324.10] |
|
| ΔfusS | 97.42 | J/mol×K | 321.30 | NIST |
| ΔfusS | 253.90 | J/mol×K | 322.00 | NIST |
| ΔfusS | 169.37 | J/mol×K | 324.10 | NIST |
| γ | [0.03; 0.03] | N/m | [333.15; 343.15] |
|
| γ | 0.03 | N/m | 333.15 | Surface... |
| γ | 0.03 | N/m | 343.15 | Surface... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 504.50 | K | 1.30 | NIST |
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.06; 101.11] | kPa | [448.15; 664.15] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 3.17065e+02 | |||
| Coefficient B | -2.83729e+04 | |||
| Coefficient C | -4.24944e+01 | |||
| Coefficient D | 1.45601e-05 | |||
| Temperature range, min. | 448.15 | |||
| Temperature range, max. | 664.15 | |||
|
T(K) Vapor pressure (kPa) 0 20 40 60 80 100 500 600 | ||||
| Pvap | 0.06 | kPa | 448.15 | Calculated Property |
| Pvap | 0.24 | kPa | 472.15 | Calculated Property |
| Pvap | 0.74 | kPa | 496.15 | Calculated Property |
| Pvap | 2.00 | kPa | 520.15 | Calculated Property |
| Pvap | 4.72 | kPa | 544.15 | Calculated Property |
| Pvap | 10.07 | kPa | 568.15 | Calculated Property |
| Pvap | 19.71 | kPa | 592.15 | Calculated Property |
| Pvap | 35.92 | kPa | 616.15 | Calculated Property |
| Pvap | 61.73 | kPa | 640.15 | Calculated Property |
| Pvap | 101.11 | kPa | 664.15 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetracosane.
Mixtures
- Tetracosane + 1-Octadecanol
- Tetracosane + 1-Eicosanol
- Tetracosane + Indole
- Tetracosane + Octane
- Tetracosane + Octane + Cyclohexane
- Tetracosane + Di-n-propyl ether
- Tetracosane + n-Butyl ether
- Tetracosane + Butane, 1-chloro-
- Tetracosane + Octane, 1-chloro-
- Tetracosane + Decane
- Tetracosane + Eicosane
- Tetracosane + Eicosane + Decane
- Toluene + Tetracosane
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Experimental solubility data of various n-alkane waxes: effects of alkane chain length, alkane odd versus even carbon number structures, and solvent chemistry on solubility
- Critical temperatures and pressures of C40, C44, and C60 normal alkanes measured by the pulse-heating technique
- Solid-liquid equilibria of eicosane, tetracosane or biphenyl + 1- octadecanol, or + 1-eicosanol mixtures
- Thermal conductivity of heavy, even-carbon number n-alkanes (C22 to C32)
- High pressure solid solid and solid liquid transition data for long chain alkanes
- Solid-liquid equilibria of indole binary systems
- Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
- A Comparison of Results by Correlation Gas Chromatography with Another Gas Chromatographic Retention Time Technique. The Effects of Retention Time Coincidence on Vaporization Enthalpy and Vapor Pressure
- Vapor Pressures and Vaporization Enthalpies of the n-Alkanes from C21 to C30 at T = 298.15 K by Correlation Gas Chromatography
- Solubilities of Some Long-Chain n-Alkanes in Dipropyl Ether, Dibutyl Ether, 1-Chlorobutane, and 1-Chlorooctane as Functions of Temperature
- Surface tension of decane binary and ternary mixtures with eicosane, docosane and tetracosane
- A Gas Saturation Apparatus for Very Low Vapor or Sublimation Pressure Measurements (10-3 Pa): Vapor-Liquid Equilibria of n-Alkanes (n-C10, n-C24, n-C28)
- Vapor and Sublimation Pressures of Three Normal Alkanes: C20, C24, and C28
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
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.