- InChI
- InChI=1S/C13H28/c1-3-5-7-9-11-13-12-10-8-6-4-2/h3-13H2,1-2H3
- InChI Key
- IIYFAKIEWZDVMP-UHFFFAOYSA-N
- Formula
- C13H28
- SMILES
- CCCCCCCCCCCCC
- Molecular Weight1
- 184.36
- CAS
- 629-50-5
- Other Names
-
- Tridecane, n-
- n-Tridecane
- 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).
- 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 standard conditions (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).
- 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).
- Tfus : Melting 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
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.6190 | KDB | |
| ΔcH°liquid | -8739.70 ± 1.40 | kJ/mol | NIST |
| ΔfG° | 58.49 | kJ/mol | KDB |
| ΔfH°gas | [-311.70; -311.50] | kJ/mol |
|
| ΔfH°gas | -311.70 | kJ/mol | KDB |
| ΔfH°gas | -311.50 ± 1.60 | kJ/mol | NIST |
| ΔfH°liquid | -377.70 ± 1.60 | kJ/mol | NIST |
| ΔfusH° | 29.43 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 91.40 | kJ/mol | NIST |
| ΔvapH° | [66.20; 66.70] | kJ/mol |
|
| ΔvapH° | 66.43 | kJ/mol | NIST |
| ΔvapH° | 66.70 | kJ/mol | NIST |
| ΔvapH° | 66.50 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 66.40 ± 0.30 | kJ/mol | NIST |
| ΔvapH° | 66.20 | kJ/mol | NIST |
| log10WS | -5.26 | Crippen Calculated Property | |
| logPoct/wat | 5.317 | Crippen Calculated Property | |
| McVol | 194.030 | ml/mol | McGowan Calculated Property |
| Pc | [1679.00; 1725.00] | kPa |
|
| Pc | 1680.00 | kPa | KDB |
| Pc | 1700.00 ± 100.00 | kPa | NIST |
| Pc | 1679.00 ± 20.00 | kPa | NIST |
| Pc | 1720.00 | kPa | NIST |
| Pc | 1725.00 ± 34.47 | kPa | NIST |
| ρc | [221.23; 224.92] | kg/m3 |
|
| ρc | 221.23 ± 18.44 | kg/m3 | NIST |
| ρc | 224.92 ± 5.53 | kg/m3 | NIST |
| Inp | [218.83; 221.55] |
|
|
| Inp | 218.83 | NIST | |
| Inp | 221.55 | NIST | |
| S°gas | 661.45 | J/mol×K | NIST |
| S°liquid | 522.87 | J/mol×K | NIST |
| Tboil | [505.00; 508.62] | K |
|
| Tboil | 508.62 | K | KDB |
| Tboil | 507.20 | K | NIST |
| Tboil | 508.60 | K | NIST |
| Tboil | 507.15 ± 0.60 | K | NIST |
| Tboil | 508.60 ± 0.30 | K | NIST |
| Tboil | 507.75 ± 0.40 | K | NIST |
| Tboil | 506.00 ± 2.00 | K | NIST |
| Tboil | 507.00 ± 1.50 | K | NIST |
| Tboil | Outlier 505.00 ± 4.00 | K | NIST |
| Tboil | 507.00 ± 4.00 | K | NIST |
| Tc | [674.00; 676.20] | K |
|
| Tc | 675.00 | K | KDB |
| Tc | 675.00 ± 1.00 | K | NIST |
| Tc | 675.80 ± 0.40 | K | NIST |
| Tc | 676.00 ± 0.60 | K | NIST |
| Tc | 675.80 ± 0.40 | K | NIST |
| Tc | 675.98 | K | NIST |
| Tc | Outlier 674.00 ± 0.80 | K | NIST |
| Tc | 675.80 | K | NIST |
| Tc | 676.20 ± 1.00 | K | NIST |
| Tc | 676.20 ± 0.60 | K | NIST |
| Tc | 674.90 ± 1.00 | K | NIST |
| Tfus | [265.00; 269.01] | K |
|
| Tfus | 267.76 | K | KDB |
| Tfus | 269.01 | K | Phase d... |
| Tfus | 269.01 | K | Influen... |
| Tfus | 267.85 ± 0.50 | K | NIST |
| Tfus | 266.00 ± 2.00 | K | NIST |
| Tfus | 267.74 ± 0.02 | K | NIST |
| Tfus | 267.74 ± 0.02 | K | NIST |
| Tfus | 267.76 ± 0.01 | K | NIST |
| Tfus | 267.00 ± 2.00 | K | NIST |
| Tfus | 267.73 ± 0.10 | K | NIST |
| Tfus | 267.76 ± 0.10 | K | NIST |
| Tfus | 267.82 ± 0.07 | K | NIST |
| Tfus | 267.80 ± 0.20 | K | NIST |
| Tfus | 267.74 ± 0.08 | K | NIST |
| Tfus | 267.74 ± 0.08 | K | NIST |
| Tfus | 267.76 ± 0.02 | K | NIST |
| Tfus | 267.90 ± 0.50 | K | NIST |
| Tfus | 267.90 ± 0.60 | K | NIST |
| Tfus | 267.70 ± 1.00 | K | NIST |
| Tfus | Outlier 265.00 ± 3.00 | K | NIST |
| Tfus | 267.00 ± 3.00 | K | NIST |
| Tfus | 266.00 ± 3.00 | K | NIST |
| Tfus | 267.00 ± 2.00 | K | NIST |
| Ttriple | [267.78; 267.79] | K |
|
| Ttriple | 267.78 ± 0.05 | K | NIST |
| Ttriple | 267.79 ± 0.02 | K | NIST |
| Ttriple | 267.78 ± 0.40 | K | NIST |
| Ttriple | 267.78 ± 0.20 | K | NIST |
| Ttriple | 267.79 ± 0.40 | K | NIST |
| Ttriple | 267.79 ± 0.20 | K | NIST |
| Vc | [0.823; 0.823] | m3/kmol |
|
| Vc | 0.823 | m3/kmol | KDB |
| Vc | 0.823 | m3/kmol | NIST |
| Zc | 0.2463590 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [455.48; 550.76] | J/mol×K | [496.84; 657.11] |
|
| Cp,gas | 455.48 | J/mol×K | 496.84 | Joback Calculated Property |
| Cp,gas | 472.94 | J/mol×K | 523.55 | Joback Calculated Property |
| Cp,gas | 489.74 | J/mol×K | 550.26 | Joback Calculated Property |
| Cp,gas | 505.91 | J/mol×K | 576.98 | Joback Calculated Property |
| Cp,gas | 521.46 | J/mol×K | 603.69 | Joback Calculated Property |
| Cp,gas | 536.40 | J/mol×K | 630.40 | Joback Calculated Property |
| Cp,gas | 550.76 | J/mol×K | 657.11 | Joback Calculated Property |
| Cp,liquid | [406.89; 409.40] | J/mol×K | [298.15; 303.15] |
|
| Cp,liquid | 406.89 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 409.40 | J/mol×K | 303.15 | NIST |
| η | [0.0001987; 0.0059922] | Pa×s | [236.27; 496.84] |
|
| η | 0.0059922 | Pa×s | 236.27 | Joback Calculated Property |
| η | 0.0021859 | Pa×s | 279.70 | Joback Calculated Property |
| η | 0.0010457 | Pa×s | 323.13 | Joback Calculated Property |
| η | 0.0005957 | Pa×s | 366.55 | Joback Calculated Property |
| η | 0.0003823 | Pa×s | 409.98 | Joback Calculated Property |
| η | 0.0002672 | Pa×s | 453.41 | Joback Calculated Property |
| η | 0.0001987 | Pa×s | 496.84 | Joback Calculated Property |
| ΔfusH | [7.66; 28.90] | kJ/mol | [255.00; 267.80] |
|
| ΔfusH | 7.66 | kJ/mol | 255.00 | NIST |
| ΔfusH | 28.90 | kJ/mol | 267.70 | NIST |
| ΔfusH | 28.49 | kJ/mol | 267.80 | NIST |
| ΔfusH | 28.49 | kJ/mol | 267.80 | NIST |
| ΔvapH | [45.65; 65.60] | kJ/mol | [308.00; 507.80] |
|
| ΔvapH | 65.60 | kJ/mol | 308.00 | NIST |
| ΔvapH | 65.30 | kJ/mol | 309.00 | NIST |
| ΔvapH | 64.90 | kJ/mol | 314.00 | NIST |
| ΔvapH | 64.60 | kJ/mol | 318.00 | NIST |
| ΔvapH | 64.20 | kJ/mol | 324.00 | NIST |
| ΔvapH | 63.30 | kJ/mol | 334.00 | NIST |
| ΔvapH | 62.40 | kJ/mol | 344.00 | NIST |
| ΔvapH | 61.70 | kJ/mol | 348.00 | NIST |
| ΔvapH | 62.30 | kJ/mol | 349.00 | NIST |
| ΔvapH | 54.50 | kJ/mol | 464.00 | NIST |
| ΔvapH | 45.65 | kJ/mol | 507.80 | KDB |
| n0 | 1.41550 | 318.15 | Thermod... | |
| ρl | [720.20; 756.00] | kg/m3 | [293.00; 344.15] |
|
| ρl | 756.00 | kg/m3 | 293.00 | KDB |
| ρl | 720.20 | kg/m3 | 344.15 | High-pr... |
| ΔfusS | [30.04; 106.27] | J/mol×K | [255.00; 267.80] |
|
| ΔfusS | 30.04 | J/mol×K | 255.00 | NIST |
| ΔfusS | 106.27 | J/mol×K | 267.80 | NIST |
| γ | [0.02; 0.03] | N/m | [293.15; 303.15] |
|
| γ | 0.02 | N/m | 293.15 | Density... |
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.02 | N/m | 303.15 | Density... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tfus | [268.21; 343.15] | K | [100.00; 495170.00] |
|
| Tfus | 268.21 | K | 100.00 | High pr... |
| Tfus | 293.15 | K | 133010.00 | High pr... |
| Tfus | 303.15 | K | 197120.00 | High pr... |
| Tfus | 313.15 | K | 265400.00 | High pr... |
| Tfus | 323.15 | K | 337830.00 | High pr... |
| Tfus | 333.15 | K | 414420.00 | High pr... |
| Tfus | 343.15 | K | 495170.00 | High pr... |
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.01 | 1023.00 | 743.49 |
| 313.01 | 2030.00 | 744.27 |
| 313.01 | 3025.00 | 745.05 |
| 313.01 | 4027.00 | 745.74 |
| 313.01 | 5014.00 | 746.51 |
| 313.01 | 6024.00 | 747.18 |
| 313.01 | 7021.00 | 747.95 |
| 313.01 | 8036.00 | 748.69 |
| 313.01 | 9019.00 | 749.41 |
| 313.01 | 10018.00 | 750.14 |
| 313.01 | 11030.00 | 750.86 |
| 313.01 | 12006.00 | 751.51 |
| 313.01 | 13017.00 | 752.24 |
| 313.01 | 14035.00 | 752.95 |
| 313.01 | 15021.00 | 753.59 |
| 313.01 | 16019.00 | 754.27 |
| 313.01 | 17019.00 | 754.94 |
| 313.01 | 18024.00 | 755.61 |
| 313.01 | 19025.00 | 756.27 |
| 313.01 | 20043.00 | 756.91 |
| 313.01 | 21011.00 | 757.52 |
| 313.01 | 22020.00 | 758.16 |
| 313.01 | 23018.00 | 758.79 |
| 313.01 | 24004.00 | 759.44 |
| 313.01 | 25036.00 | 760.12 |
| 322.92 | 1017.00 | 736.15 |
| 322.92 | 2006.00 | 736.94 |
| 322.92 | 3025.00 | 737.83 |
| 322.92 | 4021.00 | 738.62 |
| 322.92 | 5021.00 | 739.42 |
| 322.92 | 6043.00 | 740.18 |
| 322.92 | 7018.00 | 740.9 |
| 322.92 | 8022.00 | 741.72 |
| 322.92 | 9008.00 | 742.44 |
| 322.92 | 10012.00 | 743.18 |
| 322.92 | 11015.00 | 743.93 |
| 322.92 | 12006.00 | 744.71 |
| 322.92 | 13030.00 | 745.38 |
| 322.92 | 14010.00 | 746.12 |
| 322.92 | 15026.00 | 746.81 |
| 322.92 | 16024.00 | 747.53 |
| 322.92 | 17016.00 | 748.22 |
| 322.92 | 18010.00 | 748.89 |
| 322.92 | 19007.00 | 749.56 |
| 322.92 | 20023.00 | 750.22 |
| 322.92 | 21020.00 | 750.92 |
| 322.92 | 22010.00 | 751.57 |
| 322.92 | 23040.00 | 752.26 |
| 322.92 | 24006.00 | 752.95 |
| 322.92 | 25006.00 | 753.6 |
| 332.78 | 1015.00 | 729.19 |
| 332.78 | 2020.00 | 730.06 |
| 332.78 | 3022.00 | 730.83 |
| 332.78 | 4016.00 | 731.63 |
| 332.78 | 5020.00 | 732.47 |
| 332.78 | 6016.00 | 733.27 |
| 332.78 | 7006.00 | 734.09 |
| 332.78 | 8018.00 | 734.9 |
| 332.78 | 9013.00 | 735.71 |
| 332.78 | 10008.00 | 736.52 |
| 332.78 | 11016.00 | 737.3 |
| 332.78 | 12007.00 | 738.05 |
| 332.78 | 13012.00 | 738.79 |
| 332.78 | 14021.00 | 739.55 |
| 332.78 | 15011.00 | 740.26 |
| 332.78 | 16020.00 | 741.03 |
| 332.78 | 17015.00 | 741.74 |
| 332.78 | 18005.00 | 742.47 |
| 332.78 | 19017.00 | 743.19 |
| 332.78 | 20014.00 | 743.89 |
| 332.78 | 21016.00 | 744.66 |
| 332.78 | 22046.00 | 745.35 |
| 332.78 | 22994.00 | 745.97 |
| 332.78 | 24032.00 | 746.67 |
| 332.78 | 25030.00 | 747.38 |
| 342.64 | 1022.00 | 722.03 |
| 342.64 | 2014.00 | 722.93 |
| 342.64 | 3025.00 | 723.84 |
| 342.64 | 4021.00 | 724.7 |
| 342.64 | 5020.00 | 725.59 |
| 342.64 | 6020.00 | 726.44 |
| 342.64 | 7008.00 | 727.27 |
| 342.64 | 8026.00 | 728.15 |
| 342.64 | 9007.00 | 728.98 |
| 342.64 | 10010.00 | 729.81 |
| 342.64 | 11012.00 | 730.63 |
| 342.64 | 12014.00 | 731.46 |
| 342.64 | 13011.00 | 732.27 |
| 342.64 | 14008.00 | 733.03 |
| 342.64 | 15029.00 | 733.84 |
| 342.64 | 16006.00 | 734.58 |
| 342.64 | 17016.00 | 735.35 |
| 342.64 | 18019.00 | 736.09 |
| 342.64 | 19006.00 | 736.85 |
| 342.64 | 20001.00 | 737.59 |
| 342.64 | 21023.00 | 738.34 |
| 342.64 | 22008.00 | 739.06 |
| 342.64 | 23005.00 | 739.79 |
| 342.64 | 24032.00 | 740.52 |
| 342.64 | 25024.00 | 741.14 |
| 352.47 | 1013.00 | 714.88 |
| 352.47 | 2022.00 | 715.88 |
| 352.47 | 3010.00 | 716.8 |
| 352.47 | 4020.00 | 717.71 |
| 352.47 | 5019.00 | 718.65 |
| 352.47 | 6011.00 | 719.55 |
| 352.47 | 7017.00 | 720.47 |
| 352.47 | 8014.00 | 721.35 |
| 352.47 | 9022.00 | 722.24 |
| 352.47 | 10031.00 | 723.11 |
| 352.47 | 11010.00 | 723.98 |
| 352.47 | 12003.00 | 724.82 |
| 352.47 | 13024.00 | 725.71 |
| 352.47 | 14013.00 | 726.54 |
| 352.47 | 15007.00 | 727.34 |
| 352.47 | 16016.00 | 728.16 |
| 352.47 | 17007.00 | 728.94 |
| 352.47 | 18020.00 | 729.77 |
| 352.47 | 19011.00 | 730.53 |
| 352.47 | 20013.00 | 731.29 |
| 352.47 | 21032.00 | 732.07 |
| 352.47 | 22020.00 | 732.84 |
| 352.47 | 23020.00 | 733.6 |
| 352.47 | 24021.00 | 734.36 |
| 352.47 | 25024.00 | 735.14 |
| 362.25 | 1020.00 | 707.72 |
| 362.25 | 2026.00 | 708.74 |
| 362.25 | 3018.00 | 709.77 |
| 362.25 | 4006.00 | 710.71 |
| 362.25 | 5021.00 | 711.73 |
| 362.25 | 6019.00 | 712.7 |
| 362.25 | 7029.00 | 713.67 |
| 362.25 | 8017.00 | 714.54 |
| 362.25 | 9011.00 | 715.51 |
| 362.25 | 10011.00 | 716.42 |
| 362.25 | 11021.00 | 717.35 |
| 362.25 | 12018.00 | 718.24 |
| 362.25 | 13014.00 | 719.11 |
| 362.25 | 14000.00 | 719.97 |
| 362.25 | 15017.00 | 720.85 |
| 362.25 | 16026.00 | 721.7 |
| 362.25 | 17019.00 | 722.52 |
| 362.25 | 18034.00 | 723.36 |
| 362.25 | 19016.00 | 724.17 |
| 362.25 | 20004.00 | 725.0 |
| 362.25 | 21015.00 | 725.8 |
| 362.25 | 22022.00 | 726.63 |
| 362.25 | 23008.00 | 727.42 |
| 362.25 | 24034.00 | 728.22 |
| 362.25 | 25010.00 | 729.02 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 763.6 |
| 100.00 | 288.15 | 760.0 |
| 100.00 | 293.15 | 756.4 |
| 100.00 | 298.15 | 752.6 |
| 100.00 | 303.15 | 749.2 |
| 100.00 | 308.15 | 745.6 |
| 100.00 | 313.15 | 742.0 |
| 100.00 | 318.15 | 738.4 |
| 100.00 | 323.15 | 734.8 |
| 10000.00 | 283.15 | 769.7 |
| 10000.00 | 288.15 | 766.2 |
| 10000.00 | 293.15 | 762.8 |
| 10000.00 | 298.15 | 759.3 |
| 10000.00 | 303.15 | 755.9 |
| 10000.00 | 308.15 | 752.5 |
| 10000.00 | 313.15 | 749.1 |
| 10000.00 | 318.15 | 745.7 |
| 10000.00 | 323.15 | 742.3 |
| 20000.00 | 283.15 | 775.5 |
| 20000.00 | 288.15 | 772.1 |
| 20000.00 | 293.15 | 768.9 |
| 20000.00 | 298.15 | 765.5 |
| 20000.00 | 303.15 | 762.3 |
| 20000.00 | 308.15 | 759.1 |
| 20000.00 | 313.15 | 755.7 |
| 20000.00 | 318.15 | 752.5 |
| 20000.00 | 323.15 | 749.3 |
| 30000.00 | 283.15 | 781.0 |
| 30000.00 | 288.15 | 777.7 |
| 30000.00 | 293.15 | 774.6 |
| 30000.00 | 298.15 | 771.4 |
| 30000.00 | 303.15 | 768.3 |
| 30000.00 | 308.15 | 765.1 |
| 30000.00 | 313.15 | 761.9 |
| 30000.00 | 318.15 | 758.8 |
| 30000.00 | 323.15 | 755.7 |
| 40000.00 | 283.15 | 786.1 |
| 40000.00 | 288.15 | 783.0 |
| 40000.00 | 293.15 | 780.0 |
| 40000.00 | 298.15 | 776.8 |
| 40000.00 | 303.15 | 773.8 |
| 40000.00 | 308.15 | 770.8 |
| 40000.00 | 313.15 | 767.7 |
| 40000.00 | 318.15 | 764.7 |
| 40000.00 | 323.15 | 761.8 |
| 50000.00 | 283.15 | 791.0 |
| 50000.00 | 288.15 | 788.0 |
| 50000.00 | 293.15 | 785.1 |
| 50000.00 | 298.15 | 782.0 |
| 50000.00 | 303.15 | 779.0 |
| 50000.00 | 308.15 | 776.1 |
| 50000.00 | 313.15 | 773.2 |
| 50000.00 | 318.15 | 770.3 |
| 50000.00 | 323.15 | 767.3 |
| 60000.00 | 283.15 | 795.6 |
| 60000.00 | 288.15 | 792.7 |
| 60000.00 | 293.15 | 789.8 |
| 60000.00 | 298.15 | 786.9 |
| 60000.00 | 303.15 | 784.0 |
| 60000.00 | 308.15 | 781.1 |
| 60000.00 | 313.15 | 778.3 |
| 60000.00 | 318.15 | 775.4 |
| 60000.00 | 323.15 | 772.6 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.66] | kPa | [378.46; 540.38] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.48906e+01 | |||
| Coefficient B | -4.50848e+03 | |||
| Coefficient C | -6.97210e+01 | |||
| Temperature range, min. | 378.46 | |||
| Temperature range, max. | 540.38 | |||
| Pvap | 1.33 | kPa | 378.46 | Calculated Property |
| Pvap | 2.98 | kPa | 396.45 | Calculated Property |
| Pvap | 6.12 | kPa | 414.44 | Calculated Property |
| Pvap | 11.71 | kPa | 432.43 | Calculated Property |
| Pvap | 21.08 | kPa | 450.42 | Calculated Property |
| Pvap | 35.96 | kPa | 468.42 | Calculated Property |
| Pvap | 58.60 | kPa | 486.41 | Calculated Property |
| Pvap | 91.70 | kPa | 504.40 | Calculated Property |
| Pvap | 138.49 | kPa | 522.39 | Calculated Property |
| Pvap | 202.66 | kPa | 540.38 | Calculated Property |
| Pvap | [3.88e-04; 1719.36] | kPa | [267.76; 675.80] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.01620e+02 | |||
| Coefficient B | -1.09918e+04 | |||
| Coefficient C | -1.23037e+01 | |||
| Coefficient D | 4.95821e-06 | |||
| Temperature range, min. | 267.76 | |||
| Temperature range, max. | 675.80 | |||
| Pvap | 3.88e-04 | kPa | 267.76 | Calculated Property |
| Pvap | 0.02 | kPa | 313.10 | Calculated Property |
| Pvap | 0.46 | kPa | 358.44 | Calculated Property |
| Pvap | 3.95 | kPa | 403.77 | Calculated Property |
| Pvap | 20.15 | kPa | 449.11 | Calculated Property |
| Pvap | 71.97 | kPa | 494.45 | Calculated Property |
| Pvap | 199.64 | kPa | 539.79 | Calculated Property |
| Pvap | 461.69 | kPa | 585.12 | Calculated Property |
| Pvap | 935.28 | kPa | 630.46 | Calculated Property |
| Pvap | 1719.36 | kPa | 675.80 | Calculated Property |
Similar Compounds
Find more compounds similar to Tridecane.
Mixtures
- n-Hexane + Tridecane
- Tridecane + 2,3-Pentanedione
- Carbon dioxide + Tridecane
- Tridecane + Acetic acid, methyl ester
- Tridecane + Ethyl Acetate
- Tridecane + n-Propyl acetate
- Tridecane + Acetic acid, butyl ester
- Acetic acid, pentyl ester + Tridecane
- Tridecane + Methyl propionate
- Propanoic acid, ethyl ester + Tridecane
- Propanoic acid, propyl ester + Tridecane
- Propanoic acid, butyl ester + Tridecane
- Propanoic acid, pentyl ester + Tridecane
- Tridecane + Pentane, 3-methyl-
- Tridecane + Butane, 2,2-dimethyl-
- Tridecane + 1-Hexyne
- Benzene + Tridecane
- Tridecane + 4,7-Methano-1H-indene, octahydro-
- Propane, 1-nitro- + Tridecane
- Acetonitrile + Tridecane
Find more mixtures with Tridecane.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Crippen Method
- High pressure (solid + liquid) equilibria of n-alkane mixtures: experimental results, correlation and prediction
- Phase diagrams of binary systems containing n-alkanes, or cyclohexane, or 1-alkanols and 2,3-pentanedione at atmospheric and high pressure
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- High-pressure vapor liquid equilibria for CO2 + alkanol systems and densities of n-dodecane and n-tridecane
- Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- High-pressure densities and interfacial tensions of binary systems containing carbon dioxide + n-alkanes: (n-Dodecane, n-tridecane, n-tetradecane)
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Measurement and correlation of the interfacial tension for paraffin + CO2 and (CO2+N2) mixture gas at elevated temperatures and pressures
- 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
- 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 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
- Interfacial Tension Measurement and Calculation of (Carbon Dioxide + n-Alkane) Binary Mixtures
- Measurement and Correlation of High Pressure Phase Equilibria for CO2 + Alkanes and CO2 + Crude Oil Systems
- Influence of High Pressure on the Liquidus Curve Shape in Binary Hydrocarbon Mixtures: Experimental Data, Correlation, and Prediction
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- 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
- Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- (p, rho, T) Behavior for the Binary Mixtures Carbon Dioxide + Heptane and Carbon Dioxide + Tridecane
- Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
- 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
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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