- InChI
- InChI=1S/C11H24/c1-3-5-7-9-11-10-8-6-4-2/h3-11H2,1-2H3
- InChI Key
- RSJKGSCJYJTIGS-UHFFFAOYSA-N
- Formula
- C11H24
- SMILES
- CCCCCCCCCCC
- Molecular Weight1
- 156.31
- CAS
- 1120-21-4
- Other Names
-
- HENDECANE
- UN 2330
- n-C11H24
- n-Undecane
- ω : Acentric Factor.
- ΔcH°liquid : Standard liquid enthalpy of combustion (kJ/mol).
- Cp,gas : Ideal gas heat capacity (J/mol×K).
- Cp,liquid : Liquid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase 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 a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- 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).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.5350 | KDB | |
| ΔcH°liquid | [-7431.30; -7426.40] | kJ/mol |
|
| ΔcH°liquid | -7431.30 ± 2.60 | kJ/mol | NIST |
| ΔcH°liquid | -7426.40 | kJ/mol | NIST |
| μ | 0.00 | debye | KDB |
| ΔfG° | 41.62 | kJ/mol | KDB |
| ΔfH°gas | [-270.50; -270.30] | kJ/mol |
|
| ΔfH°gas | -270.50 | kJ/mol | KDB |
| ΔfH°gas | -270.30 ± 1.30 | kJ/mol | NIST |
| ΔfH°liquid | -327.20 ± 2.60 | kJ/mol | NIST |
| ΔfusH° | 24.25 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [56.30; 56.60] | kJ/mol |
|
| ΔvapH° | 56.43 | kJ/mol | NIST |
| ΔvapH° | 56.40 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 56.60 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 56.60 | kJ/mol | NIST |
| ΔvapH° | 56.44 ± 0.12 | kJ/mol | NIST |
| ΔvapH° | 56.30 | kJ/mol | NIST |
| ΔvapH° | 56.43 ± 0.08 | kJ/mol | NIST |
| ΔvapH° | 56.30 ± 0.20 | kJ/mol | NIST |
| IE | [9.45; 9.59] | eV |
|
| IE | 9.56 | eV | NIST |
| IE | 9.59 | eV | NIST |
| IE | 9.56 ± 0.10 | eV | NIST |
| IE | 9.45 ± 0.15 | eV | NIST |
| log10WS | -4.43 | Crippen Calculated Property | |
| logPoct/wat | 4.537 | Crippen Calculated Property | |
| McVol | 165.850 | ml/mol | McGowan Calculated Property |
| Pc | [1948.00; 2008.00] | kPa |
|
| Pc | 1980.00 | kPa | KDB |
| Pc | 2000.00 ± 100.00 | kPa | NIST |
| Pc | 1948.00 ± 20.00 | kPa | NIST |
| Pc | 1966.00 | kPa | NIST |
| Pc | 2008.00 ± 6.00 | kPa | NIST |
| Pc | 1990.00 ± 50.00 | kPa | NIST |
| Pc | 1966.00 ± 10.00 | kPa | NIST |
| ρc | [234.46; 276.67] | kg/m3 |
|
| ρc | 234.46 ± 15.63 | kg/m3 | NIST |
| ρc | 276.67 ± 6.25 | kg/m3 | NIST |
| Inp | [180.44; 183.23] |
|
|
| Inp | 180.44 | NIST | |
| Inp | 183.23 | NIST | |
| Inp | 180.44 | NIST | |
| S°gas | 583.58 | J/mol×K | NIST |
| S°liquid | [458.15; 464.00] | J/mol×K |
|
| S°liquid | 458.15 | J/mol×K | NIST |
| S°liquid | 464.00 | J/mol×K | NIST |
| Tboil | [466.00; 470.20] | K |
|
| Tboil | 469.09 | K | KDB |
| Tboil | 469.20 | K | NIST |
| Tboil | 468.95 ± 0.50 | K | NIST |
| Tboil | 468.55 ± 0.07 | K | NIST |
| Tboil | 468.53 ± 0.07 | K | NIST |
| Tboil | 467.95 ± 0.40 | K | NIST |
| Tboil | 468.71 ± 0.20 | K | NIST |
| Tboil | 468.65 ± 0.30 | K | NIST |
| Tboil | 467.95 ± 0.30 | K | NIST |
| Tboil | 468.00 ± 0.15 | K | NIST |
| Tboil | 470.20 ± 1.50 | K | NIST |
| Tboil | Outlier 466.00 ± 1.66 | K | NIST |
| Tboil | 470.00 ± 2.00 | K | NIST |
| Tboil | 467.65 ± 2.00 | K | NIST |
| Tboil | 469.20 ± 0.30 | K | NIST |
| Tboil | 469.04 ± 0.10 | K | NIST |
| Tboil | 469.50 ± 1.00 | K | NIST |
| Tboil | 469.10 ± 0.30 | K | NIST |
| Tboil | 468.00 ± 3.00 | K | NIST |
| Tboil | 468.70 ± 1.50 | K | NIST |
| Tboil | 468.70 ± 2.00 | K | NIST |
| Tboil | 467.70 ± 2.00 | K | NIST |
| Tboil | 469.00 ± 3.00 | K | NIST |
| Tboil | 469.20 ± 2.00 | K | NIST |
| Tboil | 468.00 ± 3.00 | K | NIST |
| Tboil | 467.60 ± 1.00 | K | NIST |
| Tboil | 470.00 ± 5.00 | K | NIST |
| Tboil | 468.99 ± 0.15 | K | NIST |
| Tboil | 467.70 ± 2.00 | K | NIST |
| Tboil | 467.70 ± 2.00 | K | NIST |
| Tboil | 468.00 ± 4.00 | K | NIST |
| Tboil | 467.00 ± 4.00 | K | NIST |
| Tboil | 467.00 ± 4.00 | K | NIST |
| Tboil | 467.00 ± 4.00 | K | NIST |
| Tboil | 467.00 ± 5.00 | K | NIST |
| Tboil | 470.00 ± 5.00 | K | NIST |
| Tboil | 470.00 ± 5.00 | K | NIST |
| Tboil | 469.00 ± 5.00 | K | NIST |
| Tboil | 470.00 ± 5.00 | K | NIST |
| Tboil | 467.70 ± 5.00 | K | NIST |
| Tc | 639.00 | K | KDB |
| Tfus | 247.50 | K | KDB |
| Ttriple | [247.20; 247.59] | K |
|
| Ttriple | 247.58 ± 0.05 | K | NIST |
| Ttriple | 247.59 ± 0.03 | K | NIST |
| Ttriple | 247.58 ± 0.20 | K | NIST |
| Ttriple | 247.59 ± 0.20 | K | NIST |
| Ttriple | 247.20 ± 0.30 | K | NIST |
| Vc | [0.689; 0.689] | m3/kmol |
|
| Vc | 0.689 | m3/kmol | KDB |
| Vc | 0.689 | m3/kmol | NIST |
| Zc | 0.2567720 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [360.07; 447.41] | J/mol×K | [451.08; 612.85] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 360 380 400 420 440 450 500 550 600 | ||||
| Cp,gas | 360.07 | J/mol×K | 451.08 | Joback Calculated Property |
| Cp,gas | 376.04 | J/mol×K | 478.04 | Joback Calculated Property |
| Cp,gas | 391.43 | J/mol×K | 505.00 | Joback Calculated Property |
| Cp,gas | 406.25 | J/mol×K | 531.96 | Joback Calculated Property |
| Cp,gas | 420.51 | J/mol×K | 558.93 | Joback Calculated Property |
| Cp,gas | 434.23 | J/mol×K | 585.89 | Joback Calculated Property |
| Cp,gas | 447.41 | J/mol×K | 612.85 | Joback Calculated Property |
| Cp,liquid | [337.29; 346.30] | J/mol×K | [283.15; 303.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 338 340 342 344 346 285 290 295 300 | ||||
| Cp,liquid | 337.29 | J/mol×K | 283.15 | Excess ... |
| Cp,liquid | 339.47 | J/mol×K | 288.15 | Excess ... |
| Cp,liquid | 341.10 | J/mol×K | 292.29 | NIST |
| Cp,liquid | 341.60 | J/mol×K | 293.15 | Excess ... |
| Cp,liquid | 342.70 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 343.98 | J/mol×K | 298.15 | Excess ... |
| Cp,liquid | 345.05 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 346.30 | J/mol×K | 303.15 | Excess ... |
| η | [0.0008780; 0.0011990] | Pa×s | [293.15; 313.15] |
|
| η | 0.0011990 | Pa×s | 293.15 | Densiti... |
| η | 0.0010990 | Pa×s | 298.15 | Densiti... |
| η | 0.0010220 | Pa×s | 303.15 | Densiti... |
| η | 0.0008780 | Pa×s | 313.15 | Densiti... |
| ΔfusH | [6.86; 22.50] | kJ/mol | [236.60; 247.60] |
|
| ΔfusH | 6.86 | kJ/mol | 236.60 | NIST |
| ΔfusH | 22.50 | kJ/mol | 247.60 | NIST |
| ΔfusH | 22.18 | kJ/mol | 247.60 | NIST |
| ΔfusH | 22.18 | kJ/mol | 247.60 | NIST |
| ΔsubH | 91.50 | kJ/mol | 236.00 | NIST |
| ΔvapH | [41.51; 60.00] | kJ/mol | [299.00; 468.70] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 40 45 50 55 60 300 350 400 450 | ||||
| ΔvapH | 56.20 | kJ/mol | 299.00 | NIST |
| ΔvapH | 55.40 | kJ/mol | 314.00 | NIST |
| ΔvapH | 54.50 | kJ/mol | 324.00 | NIST |
| ΔvapH | 54.00 | kJ/mol | 334.00 | NIST |
| ΔvapH | 53.10 | kJ/mol | 344.00 | NIST |
| ΔvapH | 60.00 | kJ/mol | 374.00 | NIST |
| ΔvapH | 49.10 | kJ/mol | 424.00 | NIST |
| ΔvapH | 41.51 | kJ/mol | 468.70 | KDB |
| Pvap | [40.00; 78.59] | kPa | [434.50; 458.59] |
|
|
T(K) Vapor pressure (kPa) 40 50 60 70 80 440 450 | ||||
| Pvap | 40.00 | kPa | 434.50 | Low-Pre... |
| Pvap | 40.04 | kPa | 434.60 | Low-Pre... |
| Pvap | 45.18 | kPa | 438.71 | Low-Pre... |
| Pvap | 50.04 | kPa | 442.20 | Low-Pre... |
| Pvap | 54.82 | kPa | 445.40 | Low-Pre... |
| Pvap | 60.13 | kPa | 448.68 | Low-Pre... |
| Pvap | 65.09 | kPa | 451.59 | Low-Pre... |
| Pvap | 70.48 | kPa | 454.55 | Low-Pre... |
| Pvap | 78.59 | kPa | 458.59 | Low-Pre... |
| n0 | [1.40630; 1.41640] | [293.15; 318.15] |
|
|
| n0 | 1.41640 | 293.15 | Activit... | |
| n0 | 1.40630 | 318.15 | Thermod... | |
| ρl | [688.18; 747.78] | kg/m3 | [283.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 690 700 710 720 730 740 750 300 320 340 360 | ||||
| ρl | 747.78 | kg/m3 | 283.15 | Densiti... |
| ρl | 747.78 | kg/m3 | 283.15 | Densiti... |
| ρl | 744.06 | kg/m3 | 288.15 | Densiti... |
| ρl | 744.06 | kg/m3 | 288.15 | Densiti... |
| ρl | 740.00 | kg/m3 | 293.00 | KDB |
| ρl | 740.35 | kg/m3 | 293.15 | Densiti... |
| ρl | 739.96 | kg/m3 | 293.15 | An Isot... |
| ρl | 740.35 | kg/m3 | 293.15 | Densiti... |
| ρl | 740.11 | kg/m3 | 293.15 | Activit... |
| ρl | 740.28 | kg/m3 | 293.15 | Excess ... |
| ρl | 737.96 | kg/m3 | 295.15 | An Isot... |
| ρl | 736.48 | kg/m3 | 297.15 | An Isot... |
| ρl | 736.73 | kg/m3 | 298.15 | Liquid-... |
| ρl | 736.64 | kg/m3 | 298.15 | Densiti... |
| ρl | 740.29 | kg/m3 | 298.15 | Liquid ... |
| ρl | 736.72 | kg/m3 | 298.15 | Liquid-... |
| ρl | 736.64 | kg/m3 | 298.15 | Densiti... |
| ρl | 736.63 | kg/m3 | 298.15 | Excess ... |
| ρl | 736.85 | kg/m3 | 298.15 | Isobari... |
| ρl | 735.73 | kg/m3 | 298.15 | An Isot... |
| ρl | 736.71 | kg/m3 | 298.15 | Thermod... |
| ρl | 736.79 | kg/m3 | 298.20 | Apparen... |
| ρl | 734.56 | kg/m3 | 299.75 | An Isot... |
| ρl | 732.93 | kg/m3 | 303.15 | Densiti... |
| ρl | 732.93 | kg/m3 | 303.15 | Excess ... |
| ρl | 732.93 | kg/m3 | 303.15 | Densiti... |
| ρl | 729.23 | kg/m3 | 308.15 | Densiti... |
| ρl | 729.22 | kg/m3 | 308.15 | Excess ... |
| ρl | 729.23 | kg/m3 | 308.15 | Densiti... |
| ρl | 725.53 | kg/m3 | 313.15 | Densiti... |
| ρl | 725.51 | kg/m3 | 313.15 | Excess ... |
| ρl | 725.53 | kg/m3 | 313.15 | Densiti... |
| ρl | 725.69 | kg/m3 | 313.20 | Apparen... |
| ρl | 721.82 | kg/m3 | 318.15 | Densiti... |
| ρl | 721.82 | kg/m3 | 318.15 | Densiti... |
| ρl | 721.82 | kg/m3 | 318.15 | Densiti... |
| ρl | 721.78 | kg/m3 | 318.15 | Excess ... |
| ρl | 718.11 | kg/m3 | 323.15 | Densiti... |
| ρl | 718.04 | kg/m3 | 323.15 | Excess ... |
| ρl | 718.11 | kg/m3 | 323.15 | Densiti... |
| ρl | 714.39 | kg/m3 | 328.15 | Densiti... |
| ρl | 714.39 | kg/m3 | 328.15 | Densiti... |
| ρl | 710.68 | kg/m3 | 333.15 | Densiti... |
| ρl | 710.68 | kg/m3 | 333.15 | Densiti... |
| ρl | 706.95 | kg/m3 | 338.15 | Densiti... |
| ρl | 706.95 | kg/m3 | 338.15 | Densiti... |
| ρl | 703.22 | kg/m3 | 343.15 | Densiti... |
| ρl | 703.22 | kg/m3 | 343.15 | Densiti... |
| ρl | 699.47 | kg/m3 | 348.15 | Densiti... |
| ρl | 699.47 | kg/m3 | 348.15 | Densiti... |
| ρl | 695.72 | kg/m3 | 353.15 | Densiti... |
| ρl | 695.72 | kg/m3 | 353.15 | Densiti... |
| ρl | 691.96 | kg/m3 | 358.15 | Densiti... |
| ρl | 691.96 | kg/m3 | 358.15 | Densiti... |
| ρl | 688.18 | kg/m3 | 363.15 | Densiti... |
| ρl | 688.18 | kg/m3 | 363.15 | Densiti... |
| ΔfusS | 29.00 | J/mol×K | 236.60 | NIST |
| γ | 0.02 | N/m | 293.20 | KDB |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 1000.00 | 278.00 | 752.64 |
| 20000.00 | 278.00 | 764.19 |
| 40000.00 | 278.00 | 775.36 |
| 60000.00 | 278.00 | 785.14 |
| 1000.00 | 288.00 | 745.18 |
| 20000.00 | 288.00 | 757.29 |
| 40000.00 | 288.00 | 768.82 |
| 60000.00 | 288.00 | 778.9 |
| 1000.00 | 298.00 | 737.58 |
| 20000.00 | 298.00 | 750.5 |
| 40000.00 | 298.00 | 762.53 |
| 60000.00 | 298.00 | 773.01 |
| 1000.00 | 308.00 | 729.86 |
| 20000.00 | 308.00 | 743.8 |
| 40000.00 | 308.00 | 756.47 |
| 60000.00 | 308.00 | 767.47 |
| 1000.00 | 318.00 | 722.02 |
| 20000.00 | 318.00 | 737.19 |
| 40000.00 | 318.00 | 750.63 |
| 60000.00 | 318.00 | 762.26 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.24 | 8029.00 | 733.14 |
| 313.18 | 9997.00 | 734.69 |
| 313.19 | 12016.00 | 736.18 |
| 313.22 | 14009.00 | 737.62 |
| 313.23 | 16006.00 | 739.05 |
| 313.19 | 18013.00 | 740.5 |
| 313.17 | 19009.00 | 741.21 |
| 323.24 | 7997.00 | 726.03 |
| 323.22 | 10009.00 | 727.67 |
| 323.23 | 12003.00 | 729.24 |
| 323.23 | 14022.00 | 730.8 |
| 323.19 | 16026.00 | 732.35 |
| 323.19 | 17995.00 | 733.8 |
| 323.18 | 19002.00 | 734.54 |
| 333.14 | 8001.00 | 718.68 |
| 333.16 | 10001.00 | 720.38 |
| 333.13 | 12007.00 | 722.07 |
| 333.15 | 14012.00 | 723.7 |
| 333.12 | 16003.00 | 725.32 |
| 333.12 | 17990.00 | 726.87 |
| 333.14 | 19027.00 | 727.66 |
| 343.29 | 7989.00 | 711.51 |
| 343.29 | 9998.00 | 713.33 |
| 343.26 | 11021.00 | 714.27 |
| 343.28 | 11999.00 | 715.12 |
| 343.25 | 13005.00 | 716.0 |
| 343.26 | 14019.00 | 716.86 |
| 343.30 | 14998.00 | 717.66 |
| 343.27 | 15997.00 | 718.51 |
| 343.25 | 16996.00 | 719.36 |
| 343.27 | 18006.00 | 720.27 |
| 343.28 | 19019.00 | 720.98 |
| 353.33 | 7993.00 | 704.36 |
| 353.35 | 9996.00 | 706.27 |
| 353.31 | 11002.00 | 707.25 |
| 353.16 | 12003.00 | 708.19 |
| 353.32 | 13007.00 | 709.08 |
| 353.33 | 14003.00 | 709.98 |
| 353.32 | 14999.00 | 710.86 |
| 353.34 | 16001.00 | 711.73 |
| 353.31 | 17012.00 | 712.63 |
| 353.33 | 18010.00 | 713.48 |
| 353.32 | 19024.00 | 714.35 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.15 | 1000.00 | 726.6 |
| 313.15 | 2001.00 | 727.3 |
| 313.15 | 3001.00 | 728.0 |
| 313.15 | 4000.00 | 728.7 |
| 313.15 | 5000.00 | 729.5 |
| 313.15 | 6001.00 | 730.2 |
| 313.15 | 7000.00 | 731.0 |
| 313.15 | 8000.00 | 731.8 |
| 313.15 | 9000.00 | 732.6 |
| 313.15 | 10000.00 | 733.4 |
| 313.15 | 11000.00 | 734.1 |
| 313.15 | 12000.00 | 734.9 |
| 313.15 | 13000.00 | 735.7 |
| 313.15 | 14001.00 | 736.4 |
| 313.15 | 15000.00 | 737.2 |
| 313.15 | 16000.00 | 737.9 |
| 313.15 | 17000.00 | 738.7 |
| 313.15 | 18000.00 | 739.4 |
| 313.15 | 19000.00 | 740.0 |
| 313.15 | 20000.00 | 740.7 |
| 313.15 | 21001.00 | 741.3 |
| 313.15 | 22000.00 | 742.0 |
| 313.15 | 23000.00 | 742.6 |
| 313.15 | 24000.00 | 743.2 |
| 313.15 | 25000.00 | 743.7 |
| 323.10 | 1000.00 | 719.0 |
| 323.10 | 2000.00 | 719.8 |
| 323.10 | 3000.00 | 720.6 |
| 323.10 | 4000.00 | 721.4 |
| 323.10 | 5001.00 | 722.2 |
| 323.10 | 6000.00 | 723.0 |
| 323.10 | 7000.00 | 723.8 |
| 323.10 | 8000.00 | 724.6 |
| 323.10 | 9000.00 | 725.5 |
| 323.10 | 10001.00 | 726.3 |
| 323.10 | 11000.00 | 727.1 |
| 323.10 | 12000.00 | 727.9 |
| 323.10 | 13000.00 | 728.7 |
| 323.10 | 14000.00 | 729.5 |
| 323.10 | 15001.00 | 730.3 |
| 323.10 | 16000.00 | 731.1 |
| 323.10 | 17000.00 | 731.9 |
| 323.10 | 18000.00 | 732.6 |
| 323.10 | 19000.00 | 733.3 |
| 323.10 | 20000.00 | 734.0 |
| 323.10 | 21000.00 | 734.7 |
| 323.10 | 22000.00 | 735.4 |
| 323.10 | 23000.00 | 736.0 |
| 323.10 | 24000.00 | 736.7 |
| 323.10 | 25000.00 | 737.3 |
| 333.02 | 1000.00 | 711.3 |
| 333.02 | 2001.00 | 712.1 |
| 333.02 | 3000.00 | 713.0 |
| 333.02 | 4000.00 | 713.8 |
| 333.02 | 5000.00 | 714.7 |
| 333.02 | 6000.00 | 715.5 |
| 333.02 | 7000.00 | 716.4 |
| 333.02 | 8001.00 | 717.3 |
| 333.02 | 9000.00 | 718.1 |
| 333.02 | 10000.00 | 719.0 |
| 333.02 | 11000.00 | 719.9 |
| 333.02 | 12000.00 | 720.7 |
| 333.02 | 13000.00 | 721.5 |
| 333.02 | 14000.00 | 722.4 |
| 333.02 | 15000.00 | 723.2 |
| 333.02 | 16000.00 | 724.0 |
| 333.02 | 17000.00 | 724.8 |
| 333.02 | 18000.00 | 725.6 |
| 333.02 | 19000.00 | 726.3 |
| 333.02 | 20000.00 | 727.1 |
| 333.02 | 21000.00 | 727.8 |
| 333.02 | 22000.00 | 728.5 |
| 333.02 | 23000.00 | 729.2 |
| 333.02 | 24000.00 | 729.9 |
| 333.02 | 25000.00 | 730.5 |
| 342.09 | 1000.00 | 703.9 |
| 342.09 | 2000.00 | 704.8 |
| 342.09 | 3001.00 | 705.8 |
| 342.09 | 4000.00 | 706.7 |
| 342.09 | 5000.00 | 707.6 |
| 342.09 | 6000.00 | 708.5 |
| 342.09 | 7000.00 | 709.4 |
| 342.09 | 8000.00 | 710.4 |
| 342.09 | 9000.00 | 711.2 |
| 342.09 | 10000.00 | 712.2 |
| 342.09 | 11000.00 | 713.1 |
| 342.09 | 12000.00 | 714.0 |
| 342.09 | 13000.00 | 714.8 |
| 342.09 | 14000.00 | 715.7 |
| 342.09 | 15000.00 | 716.6 |
| 342.09 | 16000.00 | 717.4 |
| 342.09 | 17000.00 | 718.2 |
| 342.09 | 18000.00 | 719.1 |
| 342.09 | 19000.00 | 719.9 |
| 342.09 | 20000.00 | 720.6 |
| 342.09 | 21000.00 | 721.4 |
| 342.09 | 22000.00 | 722.2 |
| 342.09 | 23000.00 | 722.9 |
| 342.09 | 23999.00 | 723.6 |
| 342.09 | 25000.00 | 724.3 |
| 352.93 | 1000.00 | 696.5 |
| 352.93 | 2000.00 | 697.4 |
| 352.93 | 3001.00 | 698.4 |
| 352.93 | 4000.00 | 699.4 |
| 352.93 | 5000.00 | 700.4 |
| 352.93 | 6000.00 | 701.4 |
| 352.93 | 7001.00 | 702.3 |
| 352.93 | 8000.00 | 703.3 |
| 352.93 | 9000.00 | 704.3 |
| 352.93 | 10001.00 | 705.2 |
| 352.93 | 11000.00 | 706.2 |
| 352.93 | 12000.00 | 707.1 |
| 352.93 | 13000.00 | 708.0 |
| 352.93 | 14000.00 | 709.0 |
| 352.93 | 15000.00 | 709.8 |
| 352.93 | 16000.00 | 710.7 |
| 352.93 | 17000.00 | 711.6 |
| 352.93 | 18000.00 | 712.5 |
| 352.93 | 19000.00 | 713.3 |
| 352.93 | 20000.00 | 714.1 |
| 352.93 | 21000.00 | 715.0 |
| 352.93 | 22000.00 | 715.7 |
| 352.93 | 23000.00 | 716.5 |
| 352.93 | 24000.00 | 717.3 |
| 352.93 | 25000.00 | 718.0 |
| 362.91 | 1000.00 | 688.8 |
| 362.91 | 2001.00 | 689.9 |
| 362.91 | 3000.00 | 691.0 |
| 362.91 | 4000.00 | 692.0 |
| 362.91 | 5001.00 | 693.1 |
| 362.91 | 6001.00 | 694.1 |
| 362.91 | 7001.00 | 695.2 |
| 362.91 | 8000.00 | 696.2 |
| 362.91 | 9000.00 | 697.2 |
| 362.91 | 10000.00 | 698.2 |
| 362.91 | 11000.00 | 699.2 |
| 362.91 | 12001.00 | 700.2 |
| 362.91 | 13000.00 | 701.1 |
| 362.91 | 14001.00 | 702.1 |
| 362.91 | 15001.00 | 703.0 |
| 362.91 | 16001.00 | 704.0 |
| 362.91 | 17001.00 | 704.9 |
| 362.91 | 18000.00 | 705.8 |
| 362.91 | 19001.00 | 706.6 |
| 362.91 | 20000.00 | 707.5 |
| 362.91 | 21000.00 | 708.4 |
| 362.91 | 22000.00 | 709.2 |
| 362.91 | 23000.00 | 710.0 |
| 362.91 | 24000.00 | 710.9 |
| 362.91 | 25000.00 | 711.6 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 747.8 |
| 100.00 | 288.15 | 744.1 |
| 100.00 | 293.15 | 740.5 |
| 100.00 | 298.15 | 736.5 |
| 100.00 | 303.15 | 732.9 |
| 100.00 | 308.15 | 729.2 |
| 100.00 | 313.15 | 725.5 |
| 100.00 | 318.15 | 721.9 |
| 100.00 | 323.15 | 718.1 |
| 10000.00 | 283.15 | 754.2 |
| 10000.00 | 288.15 | 750.7 |
| 10000.00 | 293.15 | 747.2 |
| 10000.00 | 298.15 | 743.6 |
| 10000.00 | 303.15 | 740.1 |
| 10000.00 | 308.15 | 736.7 |
| 10000.00 | 313.15 | 733.1 |
| 10000.00 | 318.15 | 729.6 |
| 10000.00 | 323.15 | 726.0 |
| 20000.00 | 283.15 | 760.4 |
| 20000.00 | 288.15 | 757.0 |
| 20000.00 | 293.15 | 753.6 |
| 20000.00 | 298.15 | 750.2 |
| 20000.00 | 303.15 | 746.8 |
| 20000.00 | 308.15 | 743.5 |
| 20000.00 | 313.15 | 740.2 |
| 20000.00 | 318.15 | 736.9 |
| 20000.00 | 323.15 | 733.5 |
| 30000.00 | 283.15 | 766.1 |
| 30000.00 | 288.15 | 762.9 |
| 30000.00 | 293.15 | 759.6 |
| 30000.00 | 298.15 | 756.4 |
| 30000.00 | 303.15 | 753.1 |
| 30000.00 | 308.15 | 749.9 |
| 30000.00 | 313.15 | 746.8 |
| 30000.00 | 318.15 | 743.5 |
| 30000.00 | 323.15 | 740.3 |
| 40000.00 | 283.15 | 771.5 |
| 40000.00 | 288.15 | 768.4 |
| 40000.00 | 293.15 | 765.3 |
| 40000.00 | 298.15 | 762.0 |
| 40000.00 | 303.15 | 758.9 |
| 40000.00 | 308.15 | 755.9 |
| 40000.00 | 313.15 | 752.9 |
| 40000.00 | 318.15 | 749.7 |
| 40000.00 | 323.15 | 746.7 |
| 50000.00 | 283.15 | 776.6 |
| 50000.00 | 288.15 | 773.5 |
| 50000.00 | 293.15 | 770.6 |
| 50000.00 | 298.15 | 767.5 |
| 50000.00 | 303.15 | 764.4 |
| 50000.00 | 308.15 | 761.4 |
| 50000.00 | 313.15 | 758.5 |
| 50000.00 | 318.15 | 755.5 |
| 50000.00 | 323.15 | 752.5 |
| 60000.00 | 283.15 | 781.4 |
| 60000.00 | 288.15 | 778.5 |
| 60000.00 | 293.15 | 775.6 |
| 60000.00 | 298.15 | 772.6 |
| 60000.00 | 303.15 | 769.7 |
| 60000.00 | 308.15 | 766.7 |
| 60000.00 | 313.15 | 763.9 |
| 60000.00 | 318.15 | 761.0 |
| 60000.00 | 323.15 | 758.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.63] | kPa | [348.32; 498.95] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45189e+01 | |||
| Coefficient B | -3.92882e+03 | |||
| Coefficient C | -7.22530e+01 | |||
| Temperature range, min. | 348.32 | |||
| Temperature range, max. | 498.95 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 500 | ||||
| Pvap | 1.33 | kPa | 348.32 | Calculated Property |
| Pvap | 3.01 | kPa | 365.06 | Calculated Property |
| Pvap | 6.21 | kPa | 381.79 | Calculated Property |
| Pvap | 11.91 | kPa | 398.53 | Calculated Property |
| Pvap | 21.44 | kPa | 415.27 | Calculated Property |
| Pvap | 36.52 | kPa | 432.00 | Calculated Property |
| Pvap | 59.35 | kPa | 448.74 | Calculated Property |
| Pvap | 92.54 | kPa | 465.48 | Calculated Property |
| Pvap | 139.14 | kPa | 482.21 | Calculated Property |
| Pvap | 202.63 | kPa | 498.95 | Calculated Property |
| Pvap | [3.78e-04; 1980.25] | kPa | [247.57; 638.76] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.34087e+02 | |||
| Coefficient B | -1.15852e+04 | |||
| Coefficient C | -1.73722e+01 | |||
| Coefficient D | 9.45325e-06 | |||
| Temperature range, min. | 247.57 | |||
| Temperature range, max. | 638.76 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 300 400 500 600 | ||||
| Pvap | 3.78e-04 | kPa | 247.57 | Calculated Property |
| Pvap | 0.03 | kPa | 291.04 | Calculated Property |
| Pvap | 0.63 | kPa | 334.50 | Calculated Property |
| Pvap | 5.40 | kPa | 377.97 | Calculated Property |
| Pvap | 26.69 | kPa | 421.43 | Calculated Property |
| Pvap | 91.24 | kPa | 464.90 | Calculated Property |
| Pvap | 242.59 | kPa | 508.36 | Calculated Property |
| Pvap | 542.83 | kPa | 551.83 | Calculated Property |
| Pvap | 1079.12 | kPa | 595.29 | Calculated Property |
| Pvap | 1980.25 | kPa | 638.76 | Calculated Property |
Similar Compounds
Find more compounds similar to Undecane.
Mixtures
- Undecane + Tributyl phosphate
- Undecane + 1-Octanamine, N,N-dioctyl-
- Undecane + p-Xylene
- Undecane + o-Xylene
- Undecane + Benzene, 1,3-dimethyl-
- Undecane + Octadecane
- Undecane + Fluoroform
- Undecane + Acetic acid, methyl ester
- Undecane + Ethyl Acetate
- Undecane + n-Propyl acetate
- Undecane + Acetic acid, butyl ester
- Undecane + Acetic acid, pentyl ester
- Undecane + Ethanol
- Undecane + Methyl propionate
- Propanoic acid, ethyl ester + Undecane
- Propanoic acid, propyl ester + Undecane
- Undecane + Propanoic acid, butyl ester
- Undecane + Propanoic acid, pentyl ester
- Undecane + Benzaldehyde, 2-hydroxy-
- Undecane + Carbon dioxide
Find more mixtures with Undecane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- New isothermal vapor liquid equilibria for the CO2 + n-nonane, and CO2 + n-undecane systems
- Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
- Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Liquid-liquid equilibria for aqueous sulfuric acid solutions with undecane, dodecane, or 1-dodecanol, trioctylamine or tributyl phosphate and excess and deviation properties for sub-binary systems at 298.15 K
- Isobaric vapor-liquid equilibrium for n-undecane + p-, o-, m-xylene at 10 kPa
- Study of critical and maximum temperatures of coexistence of liquid and gas phase in hydrocarbons binary mixtures of aromatic hydrocarbons with alkanes and cycloalkanes
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Experimental measurements and thermodynamic modeling of wax disappearance temperature for the binary systems n-C14H30 + n- C16H34, n-C16H34 + n-C18H38 and n-C11H24 + n-C18H38
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Measurement and correlation of the interfacial tension for paraffin + CO2 and (CO2+N2) mixture gas at elevated temperatures and pressures
- An Isothermal vapour-liquid equilibrium data for the binary systems of CHF3 with (n-nonane, n-decane, or n-undecane) and C2F6 with (n-nonane or n-decane)
- CO2 and alkane minimum miscible pressure estimation by the extrapolation of interfacial tension
- Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
- Liquid--liquid equilibria for mixtures of {methyl acetate + methanol + n-alkane (C10--C12)} at several temperatures and 1 atm
- Excess isobaric molar heat capacities and excess molar volumes for ethanol + n-decane and n-undecane systems
- Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
- Activity coefficients at infinite dilution of hydrocarbons, alkylbenzenes, and alcohols in the paramagnetic ionic liquid 1-butyl-3-methyl-imidazolium tetrachloridoferrate(III) using gas liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-octyl-3-methylimidazolium hexafluorophosphate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- High pressure density and speed-of-sound measurements in n-undecane and evidence of the effects of near-field diffraction
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
- Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
- Density and Volumetric Behavior of CO2 + Undecane System from 313.15 to 353.15 K and Pressures up to 19 MPa
- Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Propanol, + 1-Butanol, + 1-Pentanol, and + 1-Hexanol from 283.15 to 363.15 K at 0.1 MPa
- Densities and Viscosities for Binary Liquid Mixtures of n-Undecane + 1-Heptanol, 1-Octanol, 1-Nonanol, and 1-Decanol from 283.15 to 363.15 K at 0.1 MPa
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Vapor-Liquid-Liquid Equilibria, Azeotropic, and Excess Enthalpy Data for the Binary System n-Undecane + Propionamide, and Pure Component Vapor Pressure and Density Data for Propionamide
- Activity Coefficients at Infinite Dilution and Excess Molar Volumes in Binary Mixtures Containing Normal Alkanes (Nonane, Decane, Undecane, or Dodecane) and Cresols (2-Methylphenol or 3-Methylphenol)
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 5. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-butyl-imidazolium Bis(trifluoromethyl-sulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 6. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Methyl-3-octyl-imidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Cylcohexylamine + Octane, Toluene, Ethylbenzene, or Aniline and Excess Molar Volumes in Binary Mixtures of Cyclohexylamine + Heptane, Octane, Nonane, Decane, Undecane, Aniline, or Water
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Densities and Viscosities of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with N-Undecane or N-Tetradecane at T = (293.15 to 313.15) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Liquid Liquid Equilibria of the Ternary Systems Undecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide and Tridecane + 1,4-Diethylbenzene + Tetrahydrothiophene 1,1-Dioxide at T = (323.15, 348.15, and 373.15) K
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Densities of Cresols and Linear Alkane Mixtures at High Pressure
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- Excess Molar Volume along with Viscosity, Flash Point, and Refractive Index for Binary Mixtures of cis-Decalin or trans-Decalin with C9 to C11 n-Alkanes
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
- Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Miscibility of Trihexyl(tetradecyl)phosphonium Chloride with Alkanes
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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