- InChI
- InChI=1S/C14H30/c1-3-5-7-9-11-13-14-12-10-8-6-4-2/h3-14H2,1-2H3
- InChI Key
- BGHCVCJVXZWKCC-UHFFFAOYSA-N
- Formula
- C14H30
- SMILES
- CCCCCCCCCCCCCC
- Molecular Weight1
- 198.39
- CAS
- 629-59-4
- Other Names
-
- n-Tetradecane
- ω : Acentric Factor.
- ΔcH°gas : Standard gas 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).
- Tboilr : Boiling point at reduced pressure (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.
- 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 | 0.5810 | KDB | |
| ΔcH°gas | -9393.50 ± 1.60 | kJ/mol | NIST |
| ΔfG° | 66.86 | kJ/mol | KDB |
| ΔfH°gas | [-332.30; -332.10] | kJ/mol |
|
| ΔfH°gas | -332.30 | kJ/mol | KDB |
| ΔfH°gas | -332.10 ± 1.80 | kJ/mol | NIST |
| ΔfH°liquid | -403.30 ± 1.80 | kJ/mol | NIST |
| ΔfusH° | 32.02 | kJ/mol | Joback Calculated Property |
| ΔsubH° | 117.60 | kJ/mol | NIST |
| ΔvapH° | [71.10; 72.10] | kJ/mol |
|
| ΔvapH° | 71.30 | kJ/mol | NIST |
| ΔvapH° | 71.60 ± 1.30 | kJ/mol | NIST |
| ΔvapH° | 72.10 | kJ/mol | NIST |
| ΔvapH° | 72.00 ± 2.40 | kJ/mol | NIST |
| ΔvapH° | 71.20 | kJ/mol | NIST |
| ΔvapH° | 71.40 | kJ/mol | NIST |
| ΔvapH° | 71.70 | kJ/mol | NIST |
| ΔvapH° | 71.80 ± 0.60 | kJ/mol | NIST |
| ΔvapH° | 71.10 ± 0.40 | kJ/mol | NIST |
| ΔvapH° | 71.70 | kJ/mol | NIST |
| log10WS | [-7.96; -7.96] |
|
|
| log10WS | -7.96 | Aq. Sol... | |
| log10WS | -7.96 | Estimat... | |
| logPoct/wat | 5.707 | Crippen Calculated Property | |
| McVol | 208.120 | ml/mol | McGowan Calculated Property |
| Pc | [1438.00; 1600.00] | kPa |
|
| Pc | 1570.00 | kPa | KDB |
| Pc | 1600.00 ± 200.00 | kPa | NIST |
| Pc | 1573.00 ± 20.00 | kPa | NIST |
| Pc | 1440.00 | kPa | NIST |
| Pc | 1438.00 ± 68.94 | kPa | NIST |
| ρc | [218.23; 222.19] | kg/m3 |
|
| ρc | 218.23 ± 39.68 | kg/m3 | NIST |
| ρc | 222.19 ± 5.95 | kg/m3 | NIST |
| Inp | [236.21; 239.35] |
|
|
| Inp | 236.21 | NIST | |
| Inp | 239.35 | NIST | |
| S°gas | 700.40 | J/mol×K | NIST |
| S°liquid | [555.43; 562.30] | J/mol×K |
|
| S°liquid | 555.43 | J/mol×K | NIST |
| S°liquid | 562.30 | J/mol×K | NIST |
| Tboil | [510.00; 528.00] | K |
|
| Tboil | 526.73 | K | KDB |
| Tboil | 526.90 | K | NIST |
| Tboil | 524.15 ± 0.60 | K | NIST |
| Tboil | 525.15 ± 0.40 | K | NIST |
| Tboil | 526.40 ± 0.30 | K | NIST |
| Tboil | 528.00 ± 2.00 | K | NIST |
| Tboil | 526.04 ± 0.30 | K | NIST |
| Tboil | 512.00 ± 3.00 | K | NIST |
| Tboil | Outlier 510.00 ± 6.00 | K | NIST |
| Tboil | 525.70 ± 3.00 | K | NIST |
| Tc | [691.20; 696.90] | K |
|
| Tc | 693.00 | K | KDB |
| Tc | 693.00 ± 2.00 | K | NIST |
| Tc | 693.00 ± 1.20 | K | NIST |
| Tc | 691.80 ± 0.70 | K | NIST |
| Tc | 693.00 ± 1.20 | K | NIST |
| Tc | 692.30 | K | NIST |
| Tc | 691.20 ± 1.50 | K | NIST |
| Tc | 694.00 | K | NIST |
| Tc | 692.80 ± 1.00 | K | NIST |
| Tc | 692.80 ± 1.00 | K | NIST |
| Tc | Outlier 696.90 ± 2.00 | K | NIST |
| Tc | 694.15 ± 1.00 | K | NIST |
| Tfus | [251.00; 279.40] | K |
|
| Tfus | 279.01 | K | KDB |
| Tfus | 278.98 | K | Aq. Sol... |
| Tfus | 279.40 | K | Experim... |
| Tfus | 278.90 | K | Determi... |
| Tfus | 278.99 ± 0.05 | K | NIST |
| Tfus | 278.97 ± 0.02 | K | NIST |
| Tfus | 279.00 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 0.20 | K | NIST |
| Tfus | 279.15 ± 0.50 | K | NIST |
| Tfus | 278.70 ± 2.00 | K | NIST |
| Tfus | 278.99 ± 0.30 | K | NIST |
| Tfus | 279.00 ± 0.30 | K | NIST |
| Tfus | 278.40 ± 0.30 | K | NIST |
| Tfus | Outlier 251.00 ± 5.00 | K | NIST |
| Tfus | 279.00 ± 0.01 | K | NIST |
| Tfus | 279.00 ± 0.01 | K | NIST |
| Tfus | 279.01 ± 0.01 | K | NIST |
| Tfus | 278.90 ± 0.30 | K | NIST |
| Tfus | 278.90 ± 0.20 | K | NIST |
| Tfus | 278.92 ± 0.20 | K | NIST |
| Tfus | 279.00 ± 0.05 | K | NIST |
| Tfus | 279.01 ± 0.01 | K | NIST |
| Tfus | 277.85 ± 1.00 | K | NIST |
| Tfus | 279.01 ± 0.02 | K | NIST |
| Tfus | 279.20 ± 1.00 | K | NIST |
| Tfus | 279.20 ± 1.00 | K | NIST |
| Tfus | 278.80 ± 1.00 | K | NIST |
| Tfus | 277.40 ± 2.00 | K | NIST |
| Tfus | 278.70 ± 0.70 | K | NIST |
| Tfus | 278.00 ± 2.00 | K | NIST |
| Tfus | 278.60 ± 2.00 | K | NIST |
| Tfus | 277.70 ± 2.00 | K | NIST |
| Tfus | 277.70 ± 2.00 | K | NIST |
| Ttriple | [279.01; 279.02] | K |
|
| Ttriple | 279.02 ± 0.05 | K | NIST |
| Ttriple | 279.02 ± 0.02 | K | NIST |
| Ttriple | 279.02 ± 0.20 | K | NIST |
| Ttriple | 279.01 ± 0.20 | K | NIST |
| Vc | [0.894; 0.894] | m3/kmol |
|
| Vc | 0.894 | m3/kmol | KDB |
| Vc | 0.894 | m3/kmol | NIST |
| Zc | 0.2435940 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [505.91; 604.51] | J/mol×K | [519.72; 679.33] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 500 520 540 560 580 600 550 600 650 | ||||
| Cp,gas | 505.91 | J/mol×K | 519.72 | Joback Calculated Property |
| Cp,gas | 524.00 | J/mol×K | 546.32 | Joback Calculated Property |
| Cp,gas | 541.40 | J/mol×K | 572.92 | Joback Calculated Property |
| Cp,gas | 558.13 | J/mol×K | 599.52 | Joback Calculated Property |
| Cp,gas | 574.22 | J/mol×K | 626.13 | Joback Calculated Property |
| Cp,gas | 589.67 | J/mol×K | 652.73 | Joback Calculated Property |
| Cp,gas | 604.51 | J/mol×K | 679.33 | Joback Calculated Property |
| Cp,liquid | [433.53; 438.44] | J/mol×K | [290.60; 298.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 434 435 436 437 438 292 294 296 298 | ||||
| Cp,liquid | 434.30 | J/mol×K | 290.60 | NIST |
| Cp,liquid | 435.10 | J/mol×K | 296.20 | NIST |
| Cp,liquid | 436.00 | J/mol×K | 298.00 | NIST |
| Cp,liquid | 434.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 433.53 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 434.16 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 433.98 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 433.53 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 438.01 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 434.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 438.01 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 436.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 436.52 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 436.91 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 434.20 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 438.44 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 438.28 | J/mol×K | 298.15 | NIST |
| η | [0.0015940; 0.0023460] | Pa×s | [293.15; 313.15] |
|
| η | 0.0023460 | Pa×s | 293.15 | Densiti... |
| η | 0.0021070 | Pa×s | 298.15 | Densiti... |
| η | 0.0018970 | Pa×s | 303.15 | Densiti... |
| η | 0.0015940 | Pa×s | 313.15 | Densiti... |
| ΔfusH | [42.70; 45.07] | kJ/mol | [278.30; 279.03] |
|
| ΔfusH | 42.70 | kJ/mol | 278.30 | NIST |
| ΔfusH | 45.07 | kJ/mol | 279.00 | NIST |
| ΔfusH | 45.07 | kJ/mol | 279.00 | NIST |
| ΔfusH | 45.07 | kJ/mol | 279.03 | NIST |
| ΔvapH | [47.61; 70.10] | kJ/mol | [313.00; 526.10] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 50 55 60 65 70 350 400 450 500 | ||||
| ΔvapH | 70.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 69.00 | kJ/mol | 324.00 | NIST |
| ΔvapH | 68.90 | kJ/mol | 328.00 | NIST |
| ΔvapH | 68.60 | kJ/mol | 329.00 | NIST |
| ΔvapH | 67.90 | kJ/mol | 334.00 | NIST |
| ΔvapH | 66.80 | kJ/mol | 344.00 | NIST |
| ΔvapH | 65.70 | kJ/mol | 359.00 | NIST |
| ΔvapH | 64.10 | kJ/mol | 369.00 | NIST |
| ΔvapH | 67.80 | kJ/mol | 373.00 | NIST |
| ΔvapH | 57.80 | kJ/mol | 448.50 | NIST |
| ΔvapH | 57.10 | kJ/mol | 480.50 | NIST |
| ΔvapH | 47.61 | kJ/mol | 526.10 | KDB |
| Pvap | [4.27e-04; 50.70] | kPa | [283.15; 498.07] |
|
|
T(K) Vapor pressure (kPa) 0 10 20 30 40 50 300 400 500 | ||||
| Pvap | 4.27e-04 | kPa | 283.15 | Gas Sat... |
| Pvap | 1.21e-03 | kPa | 293.15 | Gas Sat... |
| Pvap | 3.22e-03 | kPa | 303.15 | Gas Sat... |
| Pvap | 8.10e-03 | kPa | 313.15 | Gas Sat... |
| Pvap | 0.12 | kPa | 351.75 | Isother... |
| Pvap | 0.14 | kPa | 353.15 | Isother... |
| Pvap | 0.14 | kPa | 353.15 | Isother... |
| Pvap | 0.23 | kPa | 361.80 | Isother... |
| Pvap | 0.23 | kPa | 361.89 | Isother... |
| Pvap | 0.25 | kPa | 363.15 | Isother... |
| Pvap | 0.42 | kPa | 371.91 | Isother... |
| Pvap | 0.44 | kPa | 373.15 | Isother... |
| Pvap | 0.45 | kPa | 373.15 | Isother... |
| Pvap | 0.45 | kPa | 373.15 | Isother... |
| Pvap | 0.72 | kPa | 381.93 | Isother... |
| Pvap | 0.72 | kPa | 382.07 | Isother... |
| Pvap | 0.75 | kPa | 383.15 | Isother... |
| Pvap | 0.76 | kPa | 383.15 | Isother... |
| Pvap | 0.76 | kPa | 383.15 | Isother... |
| Pvap | 1.19 | kPa | 391.95 | Isother... |
| Pvap | 1.19 | kPa | 392.00 | Isother... |
| Pvap | 1.25 | kPa | 393.15 | Isother... |
| Pvap | 1.23 | kPa | 393.15 | Isother... |
| Pvap | 1.25 | kPa | 393.15 | Isother... |
| Pvap | 1.95 | kPa | 402.74 | Isother... |
| Pvap | 1.95 | kPa | 403.15 | Isother... |
| Pvap | 2.00 | kPa | 403.15 | Isother... |
| Pvap | 3.03 | kPa | 412.69 | Isother... |
| Pvap | 3.02 | kPa | 413.15 | Isother... |
| Pvap | 3.09 | kPa | 413.15 | Isother... |
| Pvap | 3.09 | kPa | 413.15 | Isother... |
| Pvap | 4.54 | kPa | 422.55 | Isother... |
| Pvap | 4.54 | kPa | 423.15 | Isother... |
| Pvap | 4.64 | kPa | 423.15 | Isother... |
| Pvap | 4.65 | kPa | 423.15 | Isother... |
| Pvap | 6.66 | kPa | 432.39 | Isother... |
| Pvap | 6.84 | kPa | 433.15 | Isother... |
| Pvap | 6.81 | kPa | 433.15 | Isother... |
| Pvap | 6.68 | kPa | 433.15 | Isother... |
| Pvap | 9.46 | kPa | 442.49 | Isother... |
| Pvap | 9.78 | kPa | 443.15 | Isother... |
| Pvap | 9.63 | kPa | 443.15 | Isother... |
| Pvap | 13.46 | kPa | 452.49 | Isother... |
| Pvap | 13.60 | kPa | 453.15 | Isother... |
| Pvap | 13.75 | kPa | 453.15 | Isother... |
| Pvap | 40.00 | kPa | 489.17 | Low-Pre... |
| Pvap | 40.04 | kPa | 489.26 | Low-Pre... |
| Pvap | 42.42 | kPa | 491.29 | Low-Pre... |
| Pvap | 43.80 | kPa | 492.53 | Low-Pre... |
| Pvap | 46.96 | kPa | 495.18 | Low-Pre... |
| Pvap | 48.13 | kPa | 496.08 | Low-Pre... |
| Pvap | 50.50 | kPa | 497.96 | Low-Pre... |
| Pvap | 50.70 | kPa | 498.07 | Low-Pre... |
| n0 | [1.42360; 1.42910] | [293.10; 308.15] |
|
|
|
T(K) Refractive Index 1.42 1.43 1.43 1.43 1.43 1.43 295 300 305 | ||||
| n0 | 1.42910 | 293.10 | Liquid ... | |
| n0 | 1.42910 | 293.10 | Extract... | |
| n0 | 1.42890 | 293.10 | Evaluat... | |
| n0 | 1.42690 | 298.15 | Liquid-... | |
| n0 | 1.42730 | 298.15 | Measure... | |
| n0 | 1.42820 | 298.15 | Density... | |
| n0 | 1.42600 | 303.15 | Density... | |
| n0 | 1.42360 | 308.15 | Density... | |
| ρl | [727.10; 763.09] | kg/m3 | [293.00; 344.15] |
|
|
T(K) Liquid Density (kg/m3) 730 740 750 760 300 320 340 | ||||
| ρl | 763.00 | kg/m3 | 293.00 | KDB |
| ρl | 763.09 | kg/m3 | 293.15 | Excess ... |
| ρl | 759.32 | kg/m3 | 298.15 | Thermod... |
| ρl | 759.27 | kg/m3 | 298.15 | Liquid ... |
| ρl | 759.27 | kg/m3 | 298.15 | Thermod... |
| ρl | 759.38 | kg/m3 | 298.15 | Solubil... |
| ρl | 760.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 759.19 | kg/m3 | 298.15 | Thermod... |
| ρl | 759.27 | kg/m3 | 298.15 | Liquid ... |
| ρl | 759.27 | kg/m3 | 298.15 | Liquid-... |
| ρl | 759.36 | kg/m3 | 298.15 | Excess ... |
| ρl | 760.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 759.27 | kg/m3 | 298.15 | Thermod... |
| ρl | 759.27 | kg/m3 | 298.15 | Thermod... |
| ρl | 759.27 | kg/m3 | 298.15 | Liquid-... |
| ρl | 759.57 | kg/m3 | 298.15 | Excess ... |
| ρl | 759.27 | kg/m3 | 298.15 | Thermod... |
| ρl | 760.20 | kg/m3 | 298.15 | Excess ... |
| ρl | 756.03 | kg/m3 | 303.15 | Excess ... |
| ρl | 752.51 | kg/m3 | 308.15 | Excess ... |
| ρl | 748.98 | kg/m3 | 313.15 | Excess ... |
| ρl | 727.10 | kg/m3 | 344.15 | High-pr... |
| ΔfusS | 161.52 | J/mol×K | 279.03 | NIST |
| γ | [0.02; 0.03] | N/m | [293.20; 313.15] |
|
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 294.60 | Density... |
| γ | 0.02 | N/m | 313.15 | Interfa... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 395.10 | K | 1.30 | NIST |
| Tfus | [279.20; 301.70] | K | [100.00; 100000.00] |
|
|
P(kPa) Melting point (K) 280 285 290 295 300 0 50000 100000 | ||||
| Tfus | 279.20 | K | 100.00 | Liquid ... |
| Tfus | 284.20 | K | 20000.00 | Liquid ... |
| Tfus | 289.10 | K | 40000.00 | Liquid ... |
| Tfus | 293.80 | K | 60000.00 | Liquid ... |
| Tfus | 297.90 | K | 80000.00 | Liquid ... |
| Tfus | 301.70 | K | 100000.00 | Liquid ... |
Datasets
Molar heat capacity at constant pressure, J/K/mol
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Molar heat capacity at constant pressure, J/K/mol - Liquid |
| 323.15 | 120.00 | 449.55 |
| 328.15 | 120.00 | 452.72 |
| 333.15 | 120.00 | 456.09 |
| 338.15 | 120.00 | 459.47 |
| 343.15 | 120.00 | 463.04 |
| 348.15 | 120.00 | 466.61 |
| 353.15 | 120.00 | 470.38 |
| 358.15 | 120.00 | 474.15 |
| 363.15 | 120.00 | 477.72 |
| 368.15 | 120.00 | 481.49 |
| 373.15 | 120.00 | 485.26 |
| 378.15 | 120.00 | 489.03 |
| 383.15 | 120.00 | 492.80 |
| 388.15 | 120.00 | 496.76 |
| 393.15 | 120.00 | 500.14 |
| 398.15 | 120.00 | 504.50 |
| 403.15 | 120.00 | 508.27 |
| 408.15 | 120.00 | 512.44 |
| 413.15 | 120.00 | 515.81 |
| 418.15 | 120.00 | 519.58 |
| 423.15 | 120.00 | 523.35 |
| 428.15 | 120.00 | 527.12 |
| 433.15 | 120.00 | 530.89 |
| 438.15 | 120.00 | 535.25 |
| 443.15 | 120.00 | 539.81 |
| 448.15 | 120.00 | 543.58 |
| 453.15 | 120.00 | 547.95 |
| 458.15 | 120.00 | 554.10 |
| 463.15 | 120.00 | 559.65 |
| 323.15 | 10120.00 | 447.76 |
| 328.15 | 10120.00 | 451.13 |
| 333.15 | 10120.00 | 454.51 |
| 338.15 | 10120.00 | 457.88 |
| 343.15 | 10120.00 | 461.25 |
| 348.15 | 10120.00 | 464.82 |
| 353.15 | 10120.00 | 468.20 |
| 358.15 | 10120.00 | 471.97 |
| 363.15 | 10120.00 | 475.54 |
| 368.15 | 10120.00 | 478.91 |
| 373.15 | 10120.00 | 483.07 |
| 378.15 | 10120.00 | 486.45 |
| 383.15 | 10120.00 | 489.82 |
| 388.15 | 10120.00 | 493.19 |
| 393.15 | 10120.00 | 497.16 |
| 398.15 | 10120.00 | 500.73 |
| 403.15 | 10120.00 | 503.71 |
| 408.15 | 10120.00 | 508.47 |
| 413.15 | 10120.00 | 511.64 |
| 418.15 | 10120.00 | 515.41 |
| 423.15 | 10120.00 | 518.78 |
| 428.15 | 10120.00 | 522.16 |
| 433.15 | 10120.00 | 525.93 |
| 438.15 | 10120.00 | 529.30 |
| 443.15 | 10120.00 | 533.47 |
| 448.15 | 10120.00 | 537.63 |
| 453.15 | 10120.00 | 541.60 |
| 458.15 | 10120.00 | 545.77 |
| 463.15 | 10120.00 | 550.33 |
| 468.15 | 10120.00 | 553.90 |
| 473.15 | 10120.00 | 558.07 |
| 478.15 | 10120.00 | 562.83 |
| 483.15 | 10120.00 | 566.79 |
| Reference | ||
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 313.20 | 690.00 | 0.0017 |
| 313.20 | 5000.00 | 0.0017 |
| 313.20 | 10000.00 | 0.0018 |
| 313.20 | 20000.00 | 0.0020 |
| 313.20 | 30000.00 | 0.0022 |
| 313.20 | 40000.00 | 0.0025 |
| 313.20 | 50000.00 | 0.0028 |
| 313.20 | 60000.00 | 0.0031 |
| 333.20 | 690.00 | 0.0012 |
| 333.20 | 5000.00 | 0.0013 |
| 333.20 | 10000.00 | 0.0013 |
| 333.20 | 20000.00 | 0.0015 |
| 333.20 | 30000.00 | 0.0016 |
| 333.20 | 40000.00 | 0.0017 |
| 333.20 | 50000.00 | 0.0019 |
| 333.20 | 60000.00 | 0.0020 |
| 353.20 | 690.00 | 0.0009 |
| 353.20 | 5000.00 | 0.0010 |
| 353.20 | 10000.00 | 0.0010 |
| 353.20 | 20000.00 | 0.0011 |
| 353.20 | 30000.00 | 0.0012 |
| 353.20 | 40000.00 | 0.0013 |
| 353.20 | 50000.00 | 0.0014 |
| 353.20 | 60000.00 | 0.0015 |
| 373.20 | 690.00 | 0.0007 |
| 373.20 | 5000.00 | 0.0007 |
| 373.20 | 10000.00 | 0.0008 |
| 373.20 | 20000.00 | 0.0009 |
| 373.20 | 30000.00 | 0.0009 |
| 373.20 | 40000.00 | 0.0010 |
| 373.20 | 50000.00 | 0.0011 |
| 373.20 | 60000.00 | 0.0012 |
| 393.20 | 690.00 | 0.0005 |
| 393.20 | 5000.00 | 0.0006 |
| 393.20 | 10000.00 | 0.0006 |
| 393.20 | 20000.00 | 0.0007 |
| 393.20 | 30000.00 | 0.0008 |
| 393.20 | 40000.00 | 0.0008 |
| 393.20 | 50000.00 | 0.0009 |
| 393.20 | 60000.00 | 0.0010 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 294.80 | 2050.00 | 760.0 |
| 294.80 | 3540.00 | 762.0 |
| 294.40 | 5030.00 | 764.0 |
| 294.80 | 6500.00 | 765.0 |
| 294.60 | 8000.00 | 766.0 |
| 294.60 | 9490.00 | 767.0 |
| 324.10 | 2070.00 | 742.0 |
| 324.00 | 3540.00 | 743.0 |
| 324.00 | 5050.00 | 744.0 |
| 324.00 | 6560.00 | 746.0 |
| 324.10 | 8070.00 | 747.0 |
| 324.10 | 9540.00 | 748.0 |
| 373.50 | 2100.00 | 708.0 |
| 373.50 | 3560.00 | 709.0 |
| 373.30 | 5060.00 | 711.0 |
| 373.30 | 6560.00 | 712.0 |
| 373.50 | 8030.00 | 713.0 |
| 373.50 | 9500.00 | 715.0 |
| 447.60 | 1990.00 | 655.0 |
| 447.60 | 3590.00 | 658.0 |
| 447.50 | 4920.00 | 660.0 |
| 447.50 | 6450.00 | 662.0 |
| 447.60 | 7960.00 | 665.0 |
| 447.60 | 9470.00 | 667.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 100.00 | 770.0 |
| 283.15 | 470.00 | 770.2 |
| 283.15 | 960.00 | 770.5 |
| 298.15 | 100.00 | 759.4 |
| 298.15 | 470.00 | 759.7 |
| 298.15 | 960.00 | 760.0 |
| 298.15 | 2460.00 | 761.0 |
| 298.15 | 2950.00 | 761.3 |
| 298.15 | 4930.00 | 762.6 |
| 298.15 | 7410.00 | 764.2 |
| 298.15 | 9890.00 | 765.8 |
| 298.15 | 14850.00 | 768.9 |
| 298.15 | 19810.00 | 771.9 |
| 298.15 | 24770.00 | 774.8 |
| 298.15 | 29730.00 | 777.6 |
| 298.15 | 34690.00 | 780.3 |
| 298.15 | 39650.00 | 782.9 |
| 298.15 | 44610.00 | 785.4 |
| 298.15 | 49570.00 | 787.9 |
| 298.15 | 54530.00 | 790.3 |
| 298.15 | 59490.00 | 792.6 |
| 298.15 | 64450.00 | 794.9 |
| 298.15 | 69410.00 | 797.1 |
| 338.15 | 100.00 | 731.4 |
| 338.15 | 470.00 | 731.7 |
| 338.15 | 960.00 | 732.1 |
| 338.15 | 2460.00 | 733.3 |
| 338.15 | 2950.00 | 733.7 |
| 338.15 | 4930.00 | 735.3 |
| 338.15 | 7410.00 | 737.3 |
| 338.15 | 9890.00 | 739.2 |
| 338.15 | 14850.00 | 743.0 |
| 338.15 | 19810.00 | 746.5 |
| 338.15 | 29730.00 | 753.2 |
| 338.15 | 34690.00 | 756.4 |
| 338.15 | 39650.00 | 759.4 |
| 338.15 | 44610.00 | 762.4 |
| 338.15 | 49570.00 | 765.2 |
| 338.15 | 59490.00 | 770.7 |
| 338.15 | 64450.00 | 773.3 |
| 338.15 | 69410.00 | 775.8 |
| 338.15 | 44610.00 | 762.3 |
| 338.15 | 49570.00 | 765.1 |
| 338.15 | 54530.00 | 767.9 |
| 338.15 | 59490.00 | 770.6 |
| 338.15 | 64450.00 | 773.2 |
| 338.15 | 69410.00 | 775.7 |
| 288.15 | 100.00 | 766.4 |
| 288.15 | 470.00 | 766.7 |
| 288.15 | 960.00 | 766.9 |
| 288.15 | 2460.00 | 767.9 |
| 288.15 | 2950.00 | 768.2 |
| 288.15 | 4930.00 | 769.5 |
| 288.15 | 7410.00 | 771.0 |
| 288.15 | 9890.00 | 772.5 |
| 308.15 | 100.00 | 752.3 |
| 308.15 | 470.00 | 752.6 |
| 308.15 | 2460.00 | 754.0 |
| 308.15 | 4930.00 | 755.7 |
| 308.15 | 9890.00 | 759.1 |
| 308.15 | 14850.00 | 762.3 |
| 308.15 | 19810.00 | 765.4 |
| 308.15 | 24770.00 | 768.4 |
| 308.15 | 29730.00 | 771.3 |
| 308.15 | 34690.00 | 774.1 |
| 308.15 | 39650.00 | 776.9 |
| 308.15 | 44610.00 | 779.5 |
| 308.15 | 49570.00 | 782.1 |
| 308.15 | 54530.00 | 784.5 |
| 308.15 | 59490.00 | 787.0 |
| 308.15 | 64450.00 | 789.3 |
| 308.15 | 69410.00 | 791.6 |
| 358.15 | 100.00 | 717.2 |
| 358.15 | 470.00 | 717.5 |
| 358.15 | 960.00 | 718.0 |
| 358.15 | 2460.00 | 719.4 |
| 358.15 | 2950.00 | 719.8 |
| 358.15 | 4930.00 | 721.6 |
| 358.15 | 7410.00 | 723.8 |
| 358.15 | 9890.00 | 725.9 |
| 358.15 | 14850.00 | 730.0 |
| 358.15 | 19810.00 | 733.9 |
| 358.15 | 24770.00 | 737.6 |
| 358.15 | 29730.00 | 741.2 |
| 358.15 | 34690.00 | 744.6 |
| 358.15 | 39650.00 | 747.8 |
| 358.15 | 44610.00 | 751.0 |
| 358.15 | 49570.00 | 754.0 |
| 358.15 | 54530.00 | 757.0 |
| 358.15 | 59490.00 | 759.8 |
| 358.15 | 64450.00 | 762.5 |
| 358.15 | 69410.00 | 765.2 |
| 293.15 | 100.00 | 762.9 |
| 293.15 | 470.00 | 763.2 |
| 293.15 | 960.00 | 763.5 |
| 293.15 | 2460.00 | 764.5 |
| 293.15 | 2950.00 | 764.8 |
| 293.15 | 4930.00 | 766.0 |
| 293.15 | 7410.00 | 767.6 |
| 293.15 | 9890.00 | 769.2 |
| 318.15 | 100.00 | 745.4 |
| 318.15 | 470.00 | 745.6 |
| 318.15 | 960.00 | 746.0 |
| 318.15 | 2460.00 | 747.1 |
| 318.15 | 2950.00 | 747.4 |
| 318.15 | 4930.00 | 748.9 |
| 318.15 | 7410.00 | 750.7 |
| 318.15 | 9890.00 | 752.4 |
| 318.15 | 14850.00 | 755.8 |
| 318.15 | 19810.00 | 759.1 |
| 318.15 | 24770.00 | 762.3 |
| 318.15 | 29730.00 | 765.2 |
| 318.15 | 34690.00 | 768.2 |
| 318.15 | 39650.00 | 771.0 |
| 318.15 | 44610.00 | 773.8 |
| 318.15 | 49570.00 | 776.4 |
| 318.15 | 54530.00 | 779.0 |
| 318.15 | 59490.00 | 781.5 |
| 318.15 | 64450.00 | 784.0 |
| 318.15 | 69410.00 | 786.3 |
| 373.15 | 100.00 | 706.5 |
| 373.15 | 470.00 | 706.8 |
| 373.15 | 960.00 | 707.3 |
| 373.15 | 2460.00 | 708.8 |
| 373.15 | 2950.00 | 709.3 |
| 373.15 | 4930.00 | 711.3 |
| 373.15 | 7410.00 | 713.6 |
| 373.15 | 9890.00 | 715.9 |
| 373.15 | 14850.00 | 720.3 |
| 373.15 | 19810.00 | 724.5 |
| 373.15 | 24770.00 | 728.5 |
| 373.15 | 29730.00 | 732.2 |
| 373.15 | 34690.00 | 735.8 |
| 373.15 | 39650.00 | 739.3 |
| 373.15 | 44610.00 | 742.6 |
| 373.15 | 49570.00 | 745.7 |
| 373.15 | 54530.00 | 748.8 |
| 373.15 | 59490.00 | 751.8 |
| 373.15 | 64450.00 | 754.6 |
| 373.15 | 69410.00 | 757.4 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 313.19 | 10020.00 | 756.25 |
| 313.23 | 12040.00 | 757.62 |
| 313.15 | 14050.00 | 759.03 |
| 313.13 | 16040.00 | 760.35 |
| 313.15 | 18060.00 | 761.65 |
| 313.17 | 19040.00 | 762.28 |
| 323.26 | 10000.00 | 749.44 |
| 323.18 | 12040.00 | 750.93 |
| 323.14 | 14050.00 | 752.38 |
| 323.18 | 16070.00 | 753.74 |
| 323.23 | 18060.00 | 755.07 |
| 323.25 | 19080.00 | 755.76 |
| 333.14 | 10050.00 | 742.64 |
| 333.16 | 12040.00 | 744.14 |
| 333.28 | 14060.00 | 745.66 |
| 333.16 | 16060.00 | 747.18 |
| 333.13 | 18050.00 | 748.61 |
| 333.13 | 19060.00 | 749.31 |
| 343.32 | 10040.00 | 736.0 |
| 343.32 | 12050.00 | 737.59 |
| 343.35 | 14070.00 | 739.16 |
| 343.31 | 16030.00 | 740.68 |
| 343.34 | 18020.00 | 742.16 |
| 343.31 | 19040.00 | 742.92 |
| 353.63 | 10020.00 | 729.05 |
| 353.58 | 12050.00 | 730.83 |
| 353.66 | 14040.00 | 732.42 |
| 353.48 | 16030.00 | 734.17 |
| 353.50 | 18010.00 | 735.7 |
| 353.51 | 19050.00 | 736.41 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 323.20 | 1050.00 | 737.0 |
| 323.20 | 2020.00 | 742.0 |
| 323.20 | 3160.00 | 743.0 |
| 323.20 | 4070.00 | 744.0 |
| 323.20 | 5060.00 | 745.0 |
| 323.30 | 5940.00 | 745.0 |
| 373.40 | 2080.00 | 707.0 |
| 373.40 | 4050.00 | 709.0 |
| 373.40 | 6010.00 | 710.0 |
| 373.40 | 7070.00 | 711.0 |
| 373.50 | 2970.00 | 708.0 |
| 373.50 | 5010.00 | 710.0 |
| 373.60 | 1010.00 | 706.0 |
| 422.50 | 1080.00 | 672.0 |
| 422.50 | 2140.00 | 673.0 |
| 422.60 | 3020.00 | 675.0 |
| 422.60 | 4020.00 | 676.0 |
| 422.60 | 5040.00 | 677.0 |
| 422.60 | 6050.00 | 679.0 |
| 422.70 | 7000.00 | 680.0 |
| 422.70 | 8000.00 | 681.0 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 770.4 |
| 100.00 | 288.15 | 767.0 |
| 100.00 | 293.15 | 763.5 |
| 100.00 | 298.15 | 759.8 |
| 100.00 | 303.15 | 756.3 |
| 100.00 | 308.15 | 752.7 |
| 100.00 | 313.15 | 749.2 |
| 100.00 | 318.15 | 745.7 |
| 100.00 | 323.15 | 742.2 |
| 10000.00 | 283.15 | 776.4 |
| 10000.00 | 288.15 | 772.9 |
| 10000.00 | 293.15 | 769.6 |
| 10000.00 | 298.15 | 766.2 |
| 10000.00 | 303.15 | 762.8 |
| 10000.00 | 308.15 | 759.4 |
| 10000.00 | 313.15 | 756.0 |
| 10000.00 | 318.15 | 752.7 |
| 10000.00 | 323.15 | 749.4 |
| 20000.00 | 288.15 | 778.8 |
| 20000.00 | 293.15 | 775.6 |
| 20000.00 | 298.15 | 772.3 |
| 20000.00 | 303.15 | 769.0 |
| 20000.00 | 308.15 | 765.8 |
| 20000.00 | 313.15 | 762.5 |
| 20000.00 | 318.15 | 759.3 |
| 20000.00 | 323.15 | 756.2 |
| 30000.00 | 288.15 | 784.2 |
| 30000.00 | 293.15 | 781.1 |
| 30000.00 | 298.15 | 778.0 |
| 30000.00 | 303.15 | 774.8 |
| 30000.00 | 308.15 | 771.6 |
| 30000.00 | 313.15 | 768.5 |
| 30000.00 | 318.15 | 765.5 |
| 30000.00 | 323.15 | 762.4 |
| 40000.00 | 288.15 | 789.4 |
| 40000.00 | 293.15 | 786.4 |
| 40000.00 | 298.15 | 783.3 |
| 40000.00 | 303.15 | 780.2 |
| 40000.00 | 308.15 | 777.2 |
| 40000.00 | 313.15 | 774.2 |
| 40000.00 | 318.15 | 771.2 |
| 40000.00 | 323.15 | 768.4 |
| 50000.00 | 293.15 | 791.4 |
| 50000.00 | 298.15 | 788.4 |
| 50000.00 | 303.15 | 785.4 |
| 50000.00 | 308.15 | 782.4 |
| 50000.00 | 313.15 | 779.5 |
| 50000.00 | 318.15 | 776.6 |
| 50000.00 | 323.15 | 773.8 |
| 60000.00 | 293.15 | 796.1 |
| 60000.00 | 298.15 | 793.2 |
| 60000.00 | 303.15 | 790.3 |
| 60000.00 | 308.15 | 787.3 |
| 60000.00 | 313.15 | 784.5 |
| 60000.00 | 318.15 | 781.7 |
| 60000.00 | 323.15 | 779.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [395.44; 554.00] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.50005e+01 | |||
| Coefficient B | -4.49932e+03 | |||
| Coefficient C | -8.96310e+01 | |||
| Temperature range, min. | 395.44 | |||
| Temperature range, max. | 554.00 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 400 450 500 550 | ||||
| Pvap | 1.33 | kPa | 395.44 | Calculated Property |
| Pvap | 2.97 | kPa | 413.06 | Calculated Property |
| Pvap | 6.10 | kPa | 430.68 | Calculated Property |
| Pvap | 11.66 | kPa | 448.29 | Calculated Property |
| Pvap | 20.97 | kPa | 465.91 | Calculated Property |
| Pvap | 35.80 | kPa | 483.53 | Calculated Property |
| Pvap | 58.38 | kPa | 501.15 | Calculated Property |
| Pvap | 91.46 | kPa | 518.76 | Calculated Property |
| Pvap | 138.29 | kPa | 536.38 | Calculated Property |
| Pvap | 202.64 | kPa | 554.00 | Calculated Property |
| Pvap | [1.87e-04; 1663.13] | kPa | [279.01; 692.40] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 1.87822e+02 | |||
| Coefficient B | -1.58065e+04 | |||
| Coefficient C | -2.49854e+01 | |||
| Coefficient D | 1.21628e-05 | |||
| Temperature range, min. | 279.01 | |||
| Temperature range, max. | 692.40 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 400 600 | ||||
| Pvap | 1.87e-04 | kPa | 279.01 | Calculated Property |
| Pvap | 0.02 | kPa | 324.94 | Calculated Property |
| Pvap | 0.39 | kPa | 370.87 | Calculated Property |
| Pvap | 3.62 | kPa | 416.81 | Calculated Property |
| Pvap | 18.71 | kPa | 462.74 | Calculated Property |
| Pvap | 66.12 | kPa | 508.67 | Calculated Property |
| Pvap | 181.09 | kPa | 554.60 | Calculated Property |
| Pvap | 418.29 | kPa | 600.54 | Calculated Property |
| Pvap | 863.93 | kPa | 646.47 | Calculated Property |
| Pvap | 1663.13 | kPa | 692.40 | Calculated Property |
Similar Compounds
Find more compounds similar to Tetradecane.
Mixtures
- 2-Pyrrolidinone, 1-methyl- + Tetradecane
- 2-Pyrrolidinone, 1-methyl- + Benzene, propyl- + Tetradecane
- Hexadecane + Tetradecane
- Pentadecane + Tetradecane
- Benzene + Tetradecane
- Methane + Tetradecane
- Benzaldehyde + Tetradecane
- Carbon dioxide + Tetradecane
- Acetophenone + Tetradecane
- Benzyl methyl ketone + Tetradecane
- 2-Pyrrolidinone, 1-methyl- + Benzene, pentyl- + Tetradecane
- 2-Decanone + Tetradecane
- n-Amyl ether + Tetradecane
- Ethanol + Tetradecane
- Aniline, N-methyl- + Tetradecane
- Decane + Tetradecane
- Carbon dioxide + Decane + Tetradecane
- Tetradecane + Octadecane
- Tetradecane + Cyclohexane + Octadecane
- Benzene, n-butyl- + Tetradecane
Find more mixtures with Tetradecane.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- Liquid liquid equilibria for n-alkanes (C12, C14, C17) + propylbenzene +NMP mixtures at temperatures between 298 and 328K
- Liquid solid equilibria under high pressure of tetradecane + pentadecane and tetradecane + hexadecane binary systems
- Thermodynamic properties of mixtures containing ionic liquids Vapor pressures and activity coefficients of n-alcohols and benzene in binary mixtures with 1-methyl-3-butyl-imidazolium bis(trifluoromethyl-sulfonyl) imide
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Solution thermodynamics near the liquid liquid critical point I. First-order excess derivatives
- Liquid viscosities of benzene, n-tetradecane, and benzene + n-tetradecane from 313 to 393K and pressures up to 60MPa: Experiment and modeling
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Separation of propylbenzene and n-alkanes from their mixtures using 4-methyl-N-butylpyridinium tetrafluoroborate as an ionic solvent at several temperatures
- Vapor liquid equilibrium measurement and thermodynamic modeling of binary systems (methane + n-tetradecane)
- Experimental and thermodynamic modeling study on (vapor + liquid) equilibria and physical properties of ternary systems (methane + n-decane + n-tetradecane)
- Measurement and correlation of saturated liquid properties and gas solubility for decane, tetradecane and their binary mixtures saturated with carbon dioxide
- Liquid-liquid equilibria for the ternary system (water + tetradecane + 1-methyl-2-propoxyethoxy-2-propanol)
- Liquid-liquid equilibria for benzaldehyde + n-alkane mixtures andcharacterization of benzaldehyde + hydrocarbon systems in terms of DISQUAC
- 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
- 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
- Liquid liquid equilibria for acetophenone + n-alkane mixtures and characterization of acetophenone systems using DISQUAC
- Isobaric vapor-liquid equilibrium for the three binary systems of C14 - C16 n-alkane + methyl myristate at 5.00 kPa
- Thermodynamics of aromatic polar compound (alkanone, alkanal or alkanoate) + hydrocarbon mixtures
- Viscosity and density measurements on liquid n-tetradecane at moderately high pressures
- Solubility behavior of .gamma.-valerolactone + n-tetradecane or diesel mixtures at different temperatures
- CO2 and alkane minimum miscible pressure estimation by the extrapolation of interfacial tension
- Extraction of pentylbenzene from high molar mass alkanes (C14 and C17) by N-methyl-2-pyrrolidone
- Excess molar enthalpies of binary mixtures containing 2-decanone or dipentyl ether with long-chain n-alkanes at T = 298.15 K
- Interfacial tensions of binary mixtures of ethanol with octane, decane, dodecane, and tetradecane
- Evaluation of [bmim][PF6] as an ionic solvent for the extraction of propylbenzene from aliphatic compounds
- Thermodynamics of mixtures containing amines. XI. Liquid + liquid equilibria and molar excess enthalpies at 298.15 K for N-methylaniline + hydrocarbon systems. Characterization in terms of DISQUAC and ERAS models
- Phase composition and saturated liquid properties in binary and ternary systems containing carbon dioxide, n-decane, and n-tetradecane
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Measurement and correlation of solubility of carbon dioxide in triglycerides
- Super- and near-critical fluid phase behavior and phenomena of the ternary system CO2 + 1-decanol + n-tetradecane
- Heat capacity and Joule-Thomson coefficient of selected n-alkanes at 0.1 and 10 MPa in broad temperature ranges
- Determination of thermophysical properties of cyclopentane hydrate using a stirred calorimetric cell
- (p, n, T) Behavior of CO2 + Tetradecane Systems: Experiments and Thermodynamic Modeling
- Excess Molar Volumes for Three and Four Component Mixtures Simulating the Binary Mixture (Cyclohexane+ Hexadecane)
- Density, Viscosity, Speed of Sound, Bulk Modulus, Surface Tension, and Flash Point of Binary Mixtures of Butylbenzene + Linear Alkanes (n-Decane, n-Dodecane, n-Tetradecane, n-Hexadecane, or n-Heptadecane) at 0.1 MPa
- Liquid Liquid Equilibria for Systems Containing 4-Phenylbutan-2-one or Benzyl Ethanoate and Selected Alkanes
- Isothermal Vapor Pressures of Three Binary Systems: n-Tetradecane + Methyl Dodecanoate, Methyl Tetradecanoate, or Methyl Hexadecanoate between 353.15 and 453.15 K
- 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
- Liquid-Liquid Equilibria for 2-Phenylethan-1-ol + Alkane Systems
- Effect of Solvent Cation Alkyl-Chain Length on the Separation of Butylbenzene from n-Tetradecane Using Hexafluorophosphate-Based Ionic Liquids at (313.15 and 333.15) K and 101.3 kPa
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Liquid-Liquid Equilibria for Ternary Mixtures of gamma-Valerolactone + n-Tetradecane + (Butanoic Acid or Hexanoic Acid or Methyl Myristate) at 298.15 K
- Measurement and Prediction of Excess Properties of Binary Mixtures Methyl Decanoate + an Even-Numbered n-Alkane (C6-C16) at 298.15 K
- Density, Viscosity, Refractive Index, and Speed of Sound in the Binary Mixtures of Tri-n-butylamine + Triethylamine, + Tetrahydrofuran, + Tetradecane, + Tetrachloroethylene, + Pyridine, or + Trichloroethylene at (298.15, 303.15, and 308.15) K
- Excess Enthalpies of Binary Mixtures of 1-Hexene with Some n-Alkanes at 298.15 K
- Thermodynamics of Mixtures Containing Ethers. Part III. Liquid-Liquid Equilibria for 2,5,8,11-Tetraoxadodecane or 2,5,8,11,14-Pentaoxapentadecane + Selected N-Alkanes
- 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
- Liquid Liquid Equilibria of Alkane (C10 C14) + sec-Butylbenzene + Sulfolane
- Liquid Liquid Equilibria for the Ternary System Water + Tetradecane + Propylene Glycol n-Propyl Ether
- Measurement and Modeling of Liquid Saturated Properties (Solubility, Density, and Viscosity) of (Ethane + n-Tetradecane) Binary Systems
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Thermodynamics of Mixtures Containing Aromatic Alcohols. 1. Liquid Liquid Equilibria for (Phenylmethanol + Alkane) Systems
- Isothermal Vapor Liquid Equilibria of n-Tetradecane + Ethyl Hexanoate, Ethyl Decanoate, and Ethyl Tetradecanoate
- Thermodynamics of Mixtures Containing a Very Strongly Polar Compound. 10. Liquid Liquid Equilibria for N,N-Dimethylacetamide + Selected Alkanes
- Excess Molar Volumes and Viscosities of Binary Systems of Butylcyclohexane with n-Alkanes (C7 to C14) at T = 293.15 K to 313.15 K
- Thermodynamics of Mixtures Containing Amines. XV. Liquid Liquid Equilibria for Benzylamine + CH3(CH2)nCH3 (n = 8, 9, 10, 12, 14)
- Liquid-Liquid Equilibria of Alkane (C10-C14) + Hexylbenzene + Sulfolane
- Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
- Infinite Dilution Binary Diffusion Coefficients of Hydrotreating Compounds in Tetradecane in the Temperature Range from (310 to 475) K
- Thermophysical Characterization of Liquids Using Precise Density and Isobaric Heat Capacity Measurements As a Function of Pressure
- Liquid Viscosities of Cyclohexane, Cyclohexane + Tetradecane, and Cyclohexane + Benzene from (313 to 393) K and Pressures Up to 60 MPa
- Liquid Viscosities of the Ternary System Benzene + Cyclohexane + n-Tetradecane from (313 to 393) K and Pressures up to 60 MPa
- Gas Saturation Vapor Pressure Measurements of Mononitrotoluene Isomers from (283.15 to 313.15) K
- Excess Molar Enthalpies of Binary Systems of 2-Octanone or 3-Octanone with Dodecane, Tetradecane, or Hexadecane at 298.15 K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Excess Molar Enthalpies of Binary Systems of n-Valeric Anhydride or n-Hexanoic Anhydride with n-Dodecane, n-Tetradecane, or n-Hexadecane at 298.15 K
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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