- InChI
- InChI=1S/C9H20/c1-3-5-7-9-8-6-4-2/h3-9H2,1-2H3
- InChI Key
- BKIMMITUMNQMOS-UHFFFAOYSA-N
- Formula
- C9H20
- SMILES
- CCCCCCCCC
- Molecular Weight1
- 128.26
- CAS
- 111-84-2
- Other Names
-
- Shellsol 140
- UN 1920
- n-C9H20
- n-Nonane
- ω : Acentric Factor.
- Tig : Autoignition Temperature (K).
- AP : Aniline Point (K).
- 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).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Δc,grossH : Heat of Combustion, Gross form (kJ/mol).
- Δc,netH : Heat of Combustion, Net Form (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).
- NFPA Fire : NFPA Fire Rating.
- 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.
- S°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- 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 | 0.4450 | KDB | |
| Tig | 478.15 | K | KDB |
| AP | 346.850 | K | KDB |
| ΔcH°liquid | [-6125.21; -6119.80] | kJ/mol |
|
| ΔcH°liquid | -6125.21 ± 0.54 | kJ/mol | NIST |
| ΔcH°liquid | -6124.90 ± 1.10 | kJ/mol | NIST |
| ΔcH°liquid | -6119.80 | kJ/mol | NIST |
| LFL | 0.87 | % in Air | KDB |
| UFL | 2.90 | % in Air | KDB |
| Tflash,oc | 304.26 | K | KDB |
| ΔfG° | 24.83 | kJ/mol | KDB |
| Δc,grossH | 6125.17 | kJ/mol | KDB |
| Δc,netH | 5685.052 | kJ/mol | KDB |
| ΔfH°gas | [-229.20; -228.30] | kJ/mol |
|
| ΔfH°gas | -229.20 | kJ/mol | KDB |
| ΔfH°gas | -228.30 | kJ/mol | NIST |
| ΔfH°liquid | -274.70 ± 1.00 | kJ/mol | NIST |
| ΔfusH° | 19.07 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 35.63 | kJ/mol | Joback Calculated Property |
| IE | [9.63; 10.19] | eV |
|
| IE | 9.71 ± 0.10 | eV | NIST |
| IE | 9.87 | eV | NIST |
| IE | 9.71 ± 0.10 | eV | NIST |
| IE | 9.63 ± 0.15 | eV | NIST |
| IE | 10.19 | eV | NIST |
| log10WS | [-5.88; -5.88] |
|
|
| log10WS | -5.88 | Aq. Sol... | |
| log10WS | -5.88 | Estimat... | |
| logPoct/wat | 3.757 | Crippen Calculated Property | |
| McVol | 137.670 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | [2270.00; 2357.30] | kPa |
|
| Pc | 2290.00 | kPa | KDB |
| Pc | 2290.00 ± 50.00 | kPa | NIST |
| Pc | 2280.00 ± 20.00 | kPa | NIST |
| Pc | 2299.00 ± 5.00 | kPa | NIST |
| Pc | 2270.00 ± 30.00 | kPa | NIST |
| Pc | 2291.10 ± 0.22 | kPa | NIST |
| Pc | 2290.40 ± 0.22 | kPa | NIST |
| Pc | 2305.60 ± 0.23 | kPa | NIST |
| Pc | Outlier 2357.30 ± 0.23 | kPa | NIST |
| Pc | 2294.00 ± 6.89 | kPa | NIST |
| Pc | 2288.00 ± 10.00 | kPa | NIST |
| ρc | [230.86; 235.99] | kg/m3 |
|
| ρc | 230.86 ± 6.41 | kg/m3 | NIST |
| ρc | 235.99 ± 10.00 | kg/m3 | NIST |
| ρc | 230.86 ± 6.41 | kg/m3 | NIST |
| Inp | [138.27; 144.03] |
|
|
| Inp | 138.27 | NIST | |
| Inp | 144.03 | NIST | |
| Inp | 138.27 | NIST | |
| S°gas | 506.50 ± 1.00 | J/mol×K | NIST |
| S°liquid | [392.90; 393.67] | J/mol×K |
|
| S°liquid | 393.67 | J/mol×K | NIST |
| S°liquid | 392.90 | J/mol×K | NIST |
| Tboil | [421.15; 424.15] | K |
|
| Tboil | 423.97 | K | KDB |
| Tboil | 423.80 | K | Isobari... |
| Tboil | 423.80 | K | Isobari... |
| Tboil | 423.94 | K | Solutio... |
| Tboil | 423.66 | K | Densiti... |
| Tboil | 423.97 | K | Isobari... |
| Tboil | 423.94 | K | Measure... |
| Tboil | 424.00 | K | NIST |
| Tboil | 424.00 | K | NIST |
| Tboil | 423.82 ± 0.25 | K | NIST |
| Tboil | 423.88 ± 0.50 | K | NIST |
| Tboil | 424.15 ± 0.20 | K | NIST |
| Tboil | 423.90 ± 0.50 | K | NIST |
| Tboil | 423.54 ± 0.50 | K | NIST |
| Tboil | 423.20 ± 2.00 | K | NIST |
| Tboil | 423.75 ± 0.30 | K | NIST |
| Tboil | 423.91 ± 0.15 | K | NIST |
| Tboil | 423.45 ± 0.40 | K | NIST |
| Tboil | 423.45 ± 0.17 | K | NIST |
| Tboil | 423.85 ± 0.20 | K | NIST |
| Tboil | 423.45 ± 0.25 | K | NIST |
| Tboil | 423.95 ± 0.15 | K | NIST |
| Tboil | 423.65 ± 0.25 | K | NIST |
| Tboil | 423.95 ± 0.30 | K | NIST |
| Tboil | Outlier 421.65 ± 1.50 | K | NIST |
| Tboil | 423.75 ± 0.50 | K | NIST |
| Tboil | 423.80 ± 0.60 | K | NIST |
| Tboil | 423.80 ± 0.20 | K | NIST |
| Tboil | 423.80 ± 0.20 | K | NIST |
| Tboil | 422.95 ± 0.50 | K | NIST |
| Tboil | 423.92 ± 0.15 | K | NIST |
| Tboil | 423.86 ± 0.50 | K | NIST |
| Tboil | 423.90 ± 0.30 | K | NIST |
| Tboil | 423.94 ± 0.03 | K | NIST |
| Tboil | 423.05 ± 1.00 | K | NIST |
| Tboil | 423.96 ± 0.30 | K | NIST |
| Tboil | 423.95 ± 0.30 | K | NIST |
| Tboil | 423.94 ± 0.01 | K | NIST |
| Tboil | 424.00 ± 0.15 | K | NIST |
| Tboil | 424.00 ± 2.00 | K | NIST |
| Tboil | 423.65 ± 2.00 | K | NIST |
| Tboil | 424.00 ± 0.20 | K | NIST |
| Tboil | 423.95 ± 0.10 | K | NIST |
| Tboil | 423.85 ± 0.60 | K | NIST |
| Tboil | 423.85 ± 0.30 | K | NIST |
| Tboil | 423.96 ± 0.20 | K | NIST |
| Tboil | 423.40 ± 0.70 | K | NIST |
| Tboil | 423.85 ± 0.30 | K | NIST |
| Tboil | 423.70 ± 0.50 | K | NIST |
| Tboil | 423.87 ± 0.10 | K | NIST |
| Tboil | 423.86 ± 0.15 | K | NIST |
| Tboil | 423.88 ± 0.10 | K | NIST |
| Tboil | 423.86 ± 0.15 | K | NIST |
| Tboil | 423.87 ± 0.10 | K | NIST |
| Tboil | Outlier 421.15 ± 3.00 | K | NIST |
| Tboil | 423.90 ± 2.00 | K | NIST |
| Tboil | 422.65 ± 0.70 | K | NIST |
| Tboil | 422.65 ± 1.00 | K | NIST |
| Tc | [594.50; 594.60] | K |
|
| Tc | 594.60 | K | KDB |
| Tc | 594.52 | K | Experim... |
| Tc | 594.50 | K | Measure... |
| Tc | 594.52 | K | Determi... |
| Tfus | [219.60; 219.77] | K |
|
| Tfus | 219.60 | K | KDB |
| Tfus | 219.77 | K | Aq. Sol... |
| Ttriple | 219.65 | K | KDB |
| Vc | [0.555; 0.555] | m3/kmol |
|
| Vc | 0.555 | m3/kmol | KDB |
| Vc | 0.555 | m3/kmol | NIST |
| Zc | 0.2570790 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [272.67; 349.98] | J/mol×K | [405.32; 568.37] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 280 300 320 340 450 500 550 | ||||
| Cp,gas | 272.67 | J/mol×K | 405.32 | Joback Calculated Property |
| Cp,gas | 286.78 | J/mol×K | 432.50 | Joback Calculated Property |
| Cp,gas | 300.38 | J/mol×K | 459.67 | Joback Calculated Property |
| Cp,gas | 313.49 | J/mol×K | 486.85 | Joback Calculated Property |
| Cp,gas | 326.12 | J/mol×K | 514.02 | Joback Calculated Property |
| Cp,gas | 338.28 | J/mol×K | 541.20 | Joback Calculated Property |
| Cp,gas | 349.98 | J/mol×K | 568.37 | Joback Calculated Property |
| Cp,liquid | [280.13; 322.20] | J/mol×K | [288.15; 350.00] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 280 290 300 310 320 300 320 340 | ||||
| Cp,liquid | 280.13 | J/mol×K | 288.15 | Thermod... |
| Cp,liquid | 280.70 | J/mol×K | 297.90 | NIST |
| Cp,liquid | 284.39 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 284.01 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 284.34 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 284.76 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 283.80 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 284.23 | J/mol×K | 298.15 | Thermod... |
| Cp,liquid | 284.00 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 281.20 | J/mol×K | 299.10 | NIST |
| Cp,liquid | 288.80 | J/mol×K | 308.15 | Thermod... |
| Cp,liquid | 292.18 | J/mol×K | 318.15 | NIST |
| Cp,liquid | 293.20 | J/mol×K | 323.00 | NIST |
| Cp,liquid | 322.20 | J/mol×K | 350.00 | NIST |
| η | [0.0003460; 0.0009720] | Pa×s | [273.15; 358.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 3.00e-4 4.00e-4 5.00e-4 6.00e-4 7.00e-4 8.00e-4 9.00e-4 1.00e-3 300 350 | ||||
| η | 0.0009720 | Pa×s | 273.15 | Densiti... |
| η | 0.0008960 | Pa×s | 278.15 | Densiti... |
| η | 0.0008280 | Pa×s | 283.15 | Densiti... |
| η | 0.0007680 | Pa×s | 288.15 | Densiti... |
| η | 0.0007091 | Pa×s | 293.15 | Densiti... |
| η | 0.0007160 | Pa×s | 293.15 | Densiti... |
| η | 0.0006690 | Pa×s | 298.15 | Densiti... |
| η | 0.0006640 | Pa×s | 298.15 | Densiti... |
| η | 0.0006217 | Pa×s | 303.15 | Densiti... |
| η | 0.0006280 | Pa×s | 303.15 | Densiti... |
| η | 0.0005849 | Pa×s | 308.15 | Densiti... |
| η | 0.0005900 | Pa×s | 308.15 | Densiti... |
| η | 0.0005500 | Pa×s | 313.15 | Densiti... |
| η | 0.0005550 | Pa×s | 313.15 | Densiti... |
| η | 0.0005220 | Pa×s | 318.15 | Densiti... |
| η | 0.0004930 | Pa×s | 323.15 | Densiti... |
| η | 0.0004660 | Pa×s | 328.15 | Densiti... |
| η | 0.0004420 | Pa×s | 333.15 | Densiti... |
| η | 0.0004200 | Pa×s | 338.15 | Densiti... |
| η | 0.0003990 | Pa×s | 343.15 | Densiti... |
| η | 0.0003800 | Pa×s | 348.15 | Densiti... |
| η | 0.0003620 | Pa×s | 353.15 | Densiti... |
| η | 0.0003460 | Pa×s | 358.15 | Densiti... |
| ΔfusH | [15.00; 15.48] | kJ/mol | [219.50; 219.70] |
|
| ΔfusH | 15.00 | kJ/mol | 219.50 | NIST |
| ΔfusH | 15.48 | kJ/mol | 219.70 | NIST |
| ΔsubH | 74.60 | kJ/mol | 219.00 | NIST |
| ΔvapH | [36.91; 48.30] | kJ/mol | [263.50; 424.00] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 36 38 40 42 44 46 48 300 350 400 | ||||
| ΔvapH | 48.30 | kJ/mol | 263.50 | NIST |
| ΔvapH | 46.70 | kJ/mol | 299.00 | NIST |
| ΔvapH | 46.00 | kJ/mol | 314.00 | NIST |
| ΔvapH | 44.30 | kJ/mol | 328.00 | NIST |
| ΔvapH | 43.20 | kJ/mol | 343.00 | NIST |
| ΔvapH | 42.10 | kJ/mol | 358.00 | NIST |
| ΔvapH | 43.90 | kJ/mol | 367.50 | NIST |
| ΔvapH | 42.70 | kJ/mol | 385.00 | NIST |
| ΔvapH | 36.91 | kJ/mol | 423.80 | KDB |
| ΔvapH | 36.91 | kJ/mol | 424.00 | NIST |
| Pvap | [2.34; 195.54] | kPa | [322.59; 450.56] |
|
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 2.34 | kPa | 322.59 | Vapor-L... |
| Pvap | 3.97 | kPa | 333.15 | Vapor l... |
| Pvap | 4.99 | kPa | 338.33 | Vapor-L... |
| Pvap | 9.00 | kPa | 351.53 | Vapor-L... |
| Pvap | 9.65 | kPa | 353.15 | Measure... |
| Pvap | 10.28 | kPa | 353.15 | Vapor l... |
| Pvap | 15.58 | kPa | 365.30 | Measure... |
| Pvap | 18.07 | kPa | 369.25 | Measure... |
| Pvap | 19.81 | kPa | 371.37 | Vapor-L... |
| Pvap | 20.58 | kPa | 372.81 | Measure... |
| Pvap | 23.49 | kPa | 376.46 | Measure... |
| Pvap | 26.35 | kPa | 379.71 | Measure... |
| Pvap | 28.78 | kPa | 382.25 | Measure... |
| Pvap | 31.22 | kPa | 384.65 | Measure... |
| Pvap | 33.80 | kPa | 387.02 | Measure... |
| Pvap | 36.62 | kPa | 389.45 | Measure... |
| Pvap | 40.00 | kPa | 391.78 | Vapor L... |
| Pvap | 39.52 | kPa | 391.80 | Measure... |
| Pvap | 40.00 | kPa | 391.87 | Vapor L... |
| Pvap | 40.00 | kPa | 391.90 | Vapor L... |
| Pvap | 40.00 | kPa | 392.17 | Low-Pre... |
| Pvap | 39.96 | kPa | 392.77 | Low-Pre... |
| Pvap | 41.74 | kPa | 393.48 | Measure... |
| Pvap | 44.15 | kPa | 395.26 | Measure... |
| Pvap | 46.56 | kPa | 396.96 | Measure... |
| Pvap | 49.15 | kPa | 398.71 | Measure... |
| Pvap | 49.24 | kPa | 399.76 | Low-Pre... |
| Pvap | 52.12 | kPa | 400.61 | Measure... |
| Pvap | 54.42 | kPa | 402.01 | Measure... |
| Pvap | 56.55 | kPa | 403.31 | Measure... |
| Pvap | 58.04 | kPa | 404.65 | Low-Pre... |
| Pvap | 59.01 | kPa | 404.73 | Measure... |
| Pvap | 61.77 | kPa | 406.27 | Measure... |
| Pvap | 64.58 | kPa | 407.78 | Measure... |
| Pvap | 66.76 | kPa | 408.93 | Measure... |
| Pvap | 66.68 | kPa | 409.14 | Low-Pre... |
| Pvap | 69.09 | kPa | 410.11 | Measure... |
| Pvap | 71.53 | kPa | 411.32 | Measure... |
| Pvap | 74.01 | kPa | 412.52 | Measure... |
| Pvap | 75.48 | kPa | 413.23 | Low-Pre... |
| Pvap | 76.48 | kPa | 413.68 | Measure... |
| Pvap | 79.03 | kPa | 414.83 | Measure... |
| Pvap | 81.41 | kPa | 415.90 | Measure... |
| Pvap | 84.18 | kPa | 417.05 | Low-Pre... |
| Pvap | 84.44 | kPa | 417.22 | Measure... |
| Pvap | 86.85 | kPa | 418.24 | Measure... |
| Pvap | 89.41 | kPa | 419.28 | Measure... |
| Pvap | 92.43 | kPa | 420.50 | Measure... |
| Pvap | 93.72 | kPa | 420.83 | Low-Pre... |
| Pvap | 95.25 | kPa | 421.62 | Measure... |
| Pvap | 98.40 | kPa | 422.83 | Measure... |
| Pvap | 99.35 | kPa | 423.20 | Measure... |
| Pvap | 100.44 | kPa | 423.61 | Measure... |
| Pvap | 101.30 | kPa | 423.80 | Isobari... |
| Pvap | 101.70 | kPa | 423.88 | Low-Pre... |
| Pvap | 101.32 | kPa | 423.94 | Measure... |
| Pvap | 104.00 | kPa | 424.92 | Measure... |
| Pvap | 106.50 | kPa | 425.83 | Measure... |
| Pvap | 108.99 | kPa | 426.71 | Measure... |
| Pvap | 111.54 | kPa | 427.60 | Measure... |
| Pvap | 113.88 | kPa | 428.40 | Measure... |
| Pvap | 116.44 | kPa | 429.26 | Measure... |
| Pvap | 119.35 | kPa | 430.22 | Measure... |
| Pvap | 122.04 | kPa | 431.09 | Measure... |
| Pvap | 124.99 | kPa | 432.04 | Measure... |
| Pvap | 127.82 | kPa | 432.94 | Measure... |
| Pvap | 130.52 | kPa | 433.74 | Measure... |
| Pvap | 133.60 | kPa | 434.68 | Measure... |
| Pvap | 136.62 | kPa | 435.58 | Measure... |
| Pvap | 139.12 | kPa | 436.31 | Measure... |
| Pvap | 141.90 | kPa | 437.11 | Measure... |
| Pvap | 144.81 | kPa | 437.95 | Measure... |
| Pvap | 147.42 | kPa | 438.67 | Measure... |
| Pvap | 150.23 | kPa | 439.45 | Measure... |
| Pvap | 152.67 | kPa | 440.11 | Measure... |
| Pvap | 155.08 | kPa | 440.76 | Measure... |
| Pvap | 157.53 | kPa | 441.41 | Measure... |
| Pvap | 159.98 | kPa | 442.05 | Measure... |
| Pvap | 162.80 | kPa | 442.77 | Measure... |
| Pvap | 165.61 | kPa | 443.49 | Measure... |
| Pvap | 168.53 | kPa | 444.23 | Measure... |
| Pvap | 171.39 | kPa | 444.93 | Measure... |
| Pvap | 173.63 | kPa | 445.49 | Measure... |
| Pvap | 176.52 | kPa | 446.19 | Measure... |
| Pvap | 178.85 | kPa | 446.75 | Measure... |
| Pvap | 181.82 | kPa | 447.44 | Measure... |
| Pvap | 184.55 | kPa | 448.07 | Measure... |
| Pvap | 186.86 | kPa | 448.61 | Measure... |
| Pvap | 189.75 | kPa | 449.27 | Measure... |
| Pvap | 192.00 | kPa | 449.81 | Measure... |
| Pvap | 195.54 | kPa | 450.56 | Measure... |
| n0 | [1.39380; 1.40740] | [293.13; 318.15] |
|
|
|
T(K) Refractive Index 1.39 1.4 1.4 1.4 1.4 1.4 1.41 1.41 300 310 | ||||
| n0 | 1.40550 | 293.13 | Isobari... | |
| n0 | 1.40560 | 293.15 | P-rho-T... | |
| n0 | 1.40680 | 293.15 | Densiti... | |
| n0 | 1.40400 | 293.15 | Physica... | |
| n0 | 1.40550 | 293.15 | Isobari... | |
| n0 | 1.40550 | 293.15 | Activit... | |
| n0 | 1.40550 | 293.15 | Isobari... | |
| n0 | 1.40580 | 293.15 | Activit... | |
| n0 | 1.40570 | 293.15 | Infinit... | |
| n0 | 1.40740 | 293.15 | Vapor-L... | |
| n0 | 1.40550 | 293.15 | Isobari... | |
| n0 | 1.40270 | 298.15 | Physica... | |
| n0 | 1.40320 | 298.15 | Improve... | |
| n0 | 1.40310 | 298.15 | Multipr... | |
| n0 | 1.40210 | 298.15 | Excess ... | |
| n0 | 1.40320 | 298.15 | Measure... | |
| n0 | 1.40326 | 298.15 | Separat... | |
| n0 | 1.40326 | 298.15 | Liquid-... | |
| n0 | 1.40326 | 298.15 | Extract... | |
| n0 | 1.40311 | 298.15 | KDB | |
| n0 | 1.40220 | 303.15 | Densiti... | |
| n0 | 1.39980 | 303.15 | Excess ... | |
| n0 | 1.40020 | 303.15 | Physica... | |
| n0 | 1.39730 | 308.15 | Excess ... | |
| n0 | 1.39390 | 318.15 | Thermod... | |
| n0 | 1.39380 | 318.15 | Multipr... | |
| ρl | [661.14; 732.83] | kg/m3 | [273.15; 363.15] |
|
|
T(K) Liquid Density (kg/m3) 660 670 680 690 700 710 720 730 300 350 | ||||
| ρl | 732.83 | kg/m3 | 273.15 | Experim... |
| ρl | 729.01 | kg/m3 | 278.15 | Experim... |
| ρl | 725.16 | kg/m3 | 283.15 | Experim... |
| ρl | 725.58 | kg/m3 | 283.15 | Density... |
| ρl | 724.54 | kg/m3 | 285.15 | Measure... |
| ρl | 722.22 | kg/m3 | 288.15 | Measure... |
| ρl | 721.32 | kg/m3 | 288.15 | Experim... |
| ρl | 721.64 | kg/m3 | 288.15 | Densiti... |
| ρl | 718.00 | kg/m3 | 293.00 | KDB |
| ρl | 717.45 | kg/m3 | 293.15 | Experim... |
| ρl | 718.35 | kg/m3 | 293.15 | Measure... |
| ρl | 718.42 | kg/m3 | 293.15 | Liquid ... |
| ρl | 717.88 | kg/m3 | 293.15 | An Isot... |
| ρl | 717.88 | kg/m3 | 293.15 | Excess ... |
| ρl | 717.94 | kg/m3 | 293.15 | Excess ... |
| ρl | 717.86 | kg/m3 | 293.15 | Density... |
| ρl | 717.78 | kg/m3 | 293.15 | Densiti... |
| ρl | 716.60 | kg/m3 | 294.15 | An Isot... |
| ρl | 715.82 | kg/m3 | 295.15 | An Isot... |
| ρl | 715.04 | kg/m3 | 296.15 | An Isot... |
| ρl | 714.27 | kg/m3 | 297.15 | An Isot... |
| ρl | 713.91 | kg/m3 | 298.15 | Densiti... |
| ρl | 714.05 | kg/m3 | 298.15 | Liquid-... |
| ρl | 714.00 | kg/m3 | 298.15 | Excess ... |
| ρl | 714.00 | kg/m3 | 298.15 | Excess ... |
| ρl | 713.90 | kg/m3 | 298.15 | (Liquid... |
| ρl | 714.06 | kg/m3 | 298.15 | Thermod... |
| ρl | 713.58 | kg/m3 | 298.15 | Experim... |
| ρl | 713.95 | kg/m3 | 298.15 | Density... |
| ρl | 714.06 | kg/m3 | 298.15 | Thermod... |
| ρl | 714.11 | kg/m3 | 298.15 | Excess ... |
| ρl | 714.06 | kg/m3 | 298.15 | Thermod... |
| ρl | 713.99 | kg/m3 | 298.15 | Evaluat... |
| ρl | 714.46 | kg/m3 | 298.15 | Measure... |
| ρl | 713.69 | kg/m3 | 298.15 | An Isot... |
| ρl | 713.94 | kg/m3 | 298.20 | Apparen... |
| ρl | 710.20 | kg/m3 | 303.15 | Excess ... |
| ρl | 710.55 | kg/m3 | 303.15 | Measure... |
| ρl | 710.10 | kg/m3 | 303.15 | Excess ... |
| ρl | 710.03 | kg/m3 | 303.15 | Densiti... |
| ρl | 710.06 | kg/m3 | 303.15 | Density... |
| ρl | 709.69 | kg/m3 | 303.15 | Experim... |
| ρl | 705.78 | kg/m3 | 308.15 | Experim... |
| ρl | 706.19 | kg/m3 | 308.15 | Excess ... |
| ρl | 706.12 | kg/m3 | 308.15 | Densiti... |
| ρl | 706.29 | kg/m3 | 308.15 | Excess ... |
| ρl | 706.63 | kg/m3 | 308.15 | Measure... |
| ρl | 701.86 | kg/m3 | 313.15 | Experim... |
| ρl | 702.26 | kg/m3 | 313.15 | Excess ... |
| ρl | 702.20 | kg/m3 | 313.15 | Densiti... |
| ρl | 702.70 | kg/m3 | 313.15 | Measure... |
| ρl | 702.35 | kg/m3 | 313.15 | Excess ... |
| ρl | 698.26 | kg/m3 | 318.15 | Densiti... |
| ρl | 698.40 | kg/m3 | 318.15 | Excess ... |
| ρl | 697.91 | kg/m3 | 318.15 | Experim... |
| ρl | 694.43 | kg/m3 | 323.15 | Excess ... |
| ρl | 693.95 | kg/m3 | 323.15 | Experim... |
| ρl | 694.30 | kg/m3 | 323.15 | Densiti... |
| ρl | 689.97 | kg/m3 | 328.15 | Experim... |
| ρl | 690.33 | kg/m3 | 328.15 | Densiti... |
| ρl | 685.97 | kg/m3 | 333.15 | Experim... |
| ρl | 686.34 | kg/m3 | 333.15 | Densiti... |
| ρl | 681.94 | kg/m3 | 338.15 | Experim... |
| ρl | 682.31 | kg/m3 | 338.15 | Densiti... |
| ρl | 678.26 | kg/m3 | 343.15 | Densiti... |
| ρl | 677.88 | kg/m3 | 343.15 | Experim... |
| ρl | 673.91 | kg/m3 | 348.15 | Experim... |
| ρl | 669.71 | kg/m3 | 353.15 | Experim... |
| ρl | 665.58 | kg/m3 | 358.15 | Experim... |
| ρl | 661.14 | kg/m3 | 363.15 | Experim... |
| csound,fluid | [738.00; 1227.30] | m/s | [293.15; 423.15] |
|
|
T(K) Speed of sound in fluid (m/s) 700 800 900 1000 1100 1200 300 350 400 | ||||
| csound,fluid | 1227.30 | m/s | 293.15 | Tempera... |
| csound,fluid | 1207.20 | m/s | 298.15 | Tempera... |
| csound,fluid | 1187.20 | m/s | 303.15 | Tempera... |
| csound,fluid | 1167.30 | m/s | 308.15 | Tempera... |
| csound,fluid | 1147.50 | m/s | 313.15 | Tempera... |
| csound,fluid | 1127.80 | m/s | 318.15 | Tempera... |
| csound,fluid | 1108.20 | m/s | 323.15 | Tempera... |
| csound,fluid | 1088.70 | m/s | 328.15 | Tempera... |
| csound,fluid | 1069.30 | m/s | 333.15 | Tempera... |
| csound,fluid | 1050.00 | m/s | 338.15 | Tempera... |
| csound,fluid | 1030.80 | m/s | 343.15 | Tempera... |
| csound,fluid | 1011.80 | m/s | 348.15 | Tempera... |
| csound,fluid | 992.80 | m/s | 353.15 | Tempera... |
| csound,fluid | 973.90 | m/s | 358.15 | Tempera... |
| csound,fluid | 955.20 | m/s | 363.15 | Tempera... |
| csound,fluid | 936.50 | m/s | 368.15 | Tempera... |
| csound,fluid | 917.90 | m/s | 373.15 | Tempera... |
| csound,fluid | 899.50 | m/s | 378.15 | Tempera... |
| csound,fluid | 881.10 | m/s | 383.15 | Tempera... |
| csound,fluid | 862.90 | m/s | 388.15 | Tempera... |
| csound,fluid | 844.70 | m/s | 393.15 | Tempera... |
| csound,fluid | 826.70 | m/s | 398.15 | Tempera... |
| csound,fluid | 808.80 | m/s | 403.15 | Tempera... |
| csound,fluid | 790.90 | m/s | 408.15 | Tempera... |
| csound,fluid | 773.20 | m/s | 413.15 | Tempera... |
| csound,fluid | 755.60 | m/s | 418.15 | Tempera... |
| csound,fluid | 738.00 | m/s | 423.15 | Tempera... |
| γ | [0.02; 0.02] | N/m | [288.15; 323.15] |
|
|
T(K) Surface Tension (N/m) 0.02 0.02 0.02 0.02 0.02 0.02 0.02 0.02 290 300 310 320 | ||||
| γ | 0.02 | N/m | 288.15 | Density... |
| γ | 0.02 | N/m | 293.15 | Density... |
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 293.15 | Surface... |
| γ | 0.02 | N/m | 293.20 | KDB |
| γ | 0.02 | N/m | 298.15 | Density... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 303.15 | Density... |
| γ | 0.02 | N/m | 303.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Surface... |
| γ | 0.02 | N/m | 308.15 | Density... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 313.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 318.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
| γ | 0.02 | N/m | 323.15 | Surface... |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.33 | 0.0006 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 233.15 | 101.46 | 763.962 |
| 233.15 | 1176.07 | 764.563 |
| 233.15 | 2178.21 | 765.126 |
| 233.15 | 4167.03 | 766.231 |
| 233.15 | 5936.52 | 767.203 |
| 233.15 | 8144.53 | 768.395 |
| 233.15 | 10065.60 | 769.42 |
| 233.15 | 12147.70 | 770.516 |
| 233.15 | 14076.40 | 771.516 |
| 233.15 | 16087.10 | 772.548 |
| 233.15 | 18066.90 | 773.551 |
| 233.15 | 19984.50 | 774.511 |
| 233.15 | 21989.60 | 775.502 |
| 233.15 | 24043.80 | 776.506 |
| 233.15 | 25990.20 | 777.446 |
| 233.15 | 27926.70 | 778.373 |
| 233.15 | 29906.00 | 779.308 |
| 253.15 | 101.82 | 748.678 |
| 253.15 | 1135.27 | 749.335 |
| 253.15 | 2178.61 | 749.992 |
| 253.15 | 3967.76 | 751.107 |
| 253.15 | 6147.47 | 752.446 |
| 253.15 | 8137.98 | 753.648 |
| 253.15 | 10112.30 | 754.82 |
| 253.15 | 12111.20 | 755.991 |
| 253.15 | 14130.20 | 757.156 |
| 253.15 | 16140.10 | 758.299 |
| 253.15 | 18106.10 | 759.398 |
| 253.15 | 20064.20 | 760.484 |
| 253.15 | 22026.10 | 761.552 |
| 253.15 | 23955.00 | 762.59 |
| 253.15 | 25972.30 | 763.661 |
| 253.15 | 27912.60 | 764.677 |
| 253.15 | 29966.80 | 765.739 |
| 273.15 | 102.52 | 733.389 |
| 273.15 | 1156.84 | 734.143 |
| 273.15 | 2137.97 | 734.842 |
| 273.15 | 4026.01 | 736.166 |
| 273.15 | 6169.44 | 737.644 |
| 273.15 | 8161.45 | 738.99 |
| 273.15 | 10122.00 | 740.29 |
| 273.15 | 12106.50 | 741.586 |
| 273.15 | 14100.70 | 742.864 |
| 273.15 | 16067.00 | 744.108 |
| 273.15 | 18074.30 | 745.354 |
| 273.15 | 20036.30 | 746.555 |
| 273.15 | 21999.70 | 747.737 |
| 273.15 | 23995.50 | 748.923 |
| 273.15 | 25993.50 | 750.093 |
| 273.15 | 27981.50 | 751.238 |
| 273.15 | 29875.50 | 752.316 |
| 293.15 | 101.69 | 717.968 |
| 293.15 | 1184.28 | 718.847 |
| 293.15 | 2129.17 | 719.604 |
| 293.15 | 3960.49 | 721.055 |
| 293.15 | 6115.45 | 722.729 |
| 293.15 | 7981.56 | 724.145 |
| 293.15 | 10014.70 | 725.663 |
| 293.15 | 12148.60 | 727.214 |
| 293.15 | 13981.10 | 728.526 |
| 293.15 | 16170.10 | 730.062 |
| 293.15 | 17942.90 | 731.285 |
| 293.15 | 20200.00 | 732.813 |
| 293.15 | 22156.50 | 734.115 |
| 293.15 | 24157.90 | 735.421 |
| 293.15 | 26136.50 | 736.696 |
| 293.15 | 28126.30 | 737.958 |
| 293.15 | 29978.50 | 739.115 |
| 313.15 | 98.73 | 702.339 |
| 313.15 | 1168.73 | 703.323 |
| 313.15 | 2131.95 | 704.205 |
| 313.15 | 3967.37 | 705.852 |
| 313.15 | 6162.29 | 707.777 |
| 313.15 | 8113.86 | 709.449 |
| 313.15 | 10023.50 | 711.038 |
| 313.15 | 12172.80 | 712.791 |
| 313.15 | 14170.00 | 714.384 |
| 313.15 | 16194.40 | 715.964 |
| 313.15 | 17956.10 | 717.315 |
| 313.15 | 20057.40 | 718.889 |
| 313.15 | 22190.80 | 720.459 |
| 313.15 | 24136.30 | 721.862 |
| 313.15 | 26139.10 | 723.282 |
| 313.15 | 28073.10 | 724.629 |
| 313.15 | 29972.40 | 725.932 |
| 333.15 | 102.84 | 686.431 |
| 333.15 | 1137.45 | 687.521 |
| 333.15 | 2113.93 | 688.539 |
| 333.15 | 4162.71 | 690.632 |
| 333.15 | 6145.33 | 692.599 |
| 333.15 | 8151.89 | 694.535 |
| 333.15 | 10023.60 | 696.296 |
| 333.15 | 12113.90 | 698.208 |
| 333.15 | 14126.60 | 700.005 |
| 333.15 | 15989.20 | 701.627 |
| 333.15 | 18027.40 | 703.362 |
| 333.15 | 19954.20 | 704.977 |
| 333.15 | 22112.40 | 706.723 |
| 333.15 | 24079.90 | 708.292 |
| 333.15 | 26037.60 | 709.821 |
| 333.15 | 28054.20 | 711.366 |
| 333.15 | 29912.30 | 712.772 |
| 353.15 | 97.13 | 671.217 |
| 353.15 | 2136.70 | 672.617 |
| 353.15 | 6141.90 | 677.222 |
| 353.15 | 8110.87 | 679.378 |
| 353.15 | 10054.10 | 681.439 |
| 353.15 | 12124.00 | 683.57 |
| 353.15 | 14143.80 | 685.589 |
| 353.15 | 15989.00 | 687.385 |
| 353.15 | 18010.60 | 689.305 |
| 353.15 | 20035.80 | 691.174 |
| 353.15 | 21991.10 | 692.938 |
| 353.15 | 23964.80 | 694.678 |
| 353.15 | 25968.30 | 696.403 |
| 353.15 | 27955.30 | 698.078 |
| 353.15 | 29938.70 | 699.718 |
| 373.15 | 102.37 | 653.427 |
| 373.15 | 1227.94 | 655.018 |
| 373.15 | 2148.86 | 656.298 |
| 373.15 | 4131.53 | 658.968 |
| 373.15 | 6127.03 | 661.551 |
| 373.15 | 8138.76 | 664.058 |
| 373.15 | 10022.20 | 666.323 |
| 373.15 | 12111.60 | 668.749 |
| 373.15 | 14118.80 | 671.003 |
| 373.15 | 16133.90 | 673.197 |
| 373.15 | 18104.00 | 675.276 |
| 373.15 | 20078.30 | 677.302 |
| 373.15 | 22063.50 | 679.286 |
| 373.15 | 23987.70 | 681.158 |
| 373.15 | 26124.00 | 683.184 |
| 373.15 | 28010.20 | 684.93 |
| 373.15 | 29904.70 | 686.647 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 298.15 | 713.93 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 283.15 | 1010.00 | 726.22 |
| 283.15 | 5040.00 | 729.17 |
| 283.15 | 10020.00 | 732.75 |
| 283.15 | 15020.00 | 736.14 |
| 283.15 | 20040.00 | 739.41 |
| 283.15 | 25020.00 | 742.54 |
| 283.15 | 30040.00 | 745.52 |
| 283.15 | 35050.00 | 748.45 |
| 283.15 | 40010.00 | 751.23 |
| 283.15 | 45050.00 | 753.99 |
| 283.15 | 50010.00 | 756.62 |
| 283.15 | 55020.00 | 759.19 |
| 283.15 | 60030.00 | 761.66 |
| 283.15 | 65010.00 | 764.08 |
| 283.15 | 5020.00 | 729.22 |
| 298.15 | 1020.00 | 714.83 |
| 298.15 | 5010.00 | 718.08 |
| 298.15 | 10030.00 | 721.94 |
| 298.15 | 15060.00 | 725.7 |
| 298.15 | 20040.00 | 729.17 |
| 298.15 | 25040.00 | 732.54 |
| 298.15 | 30010.00 | 735.76 |
| 298.15 | 35050.00 | 738.87 |
| 298.15 | 40010.00 | 741.88 |
| 298.15 | 45060.00 | 744.79 |
| 298.15 | 50010.00 | 747.56 |
| 298.15 | 55040.00 | 750.31 |
| 298.15 | 60020.00 | 752.92 |
| 298.15 | 65010.00 | 755.48 |
| 298.15 | 5040.00 | 718.12 |
| 323.15 | 1030.00 | 695.27 |
| 323.15 | 5030.00 | 699.04 |
| 323.15 | 10050.00 | 703.57 |
| 323.15 | 15020.00 | 707.81 |
| 323.15 | 20050.00 | 711.84 |
| 323.15 | 25020.00 | 715.63 |
| 323.15 | 30020.00 | 719.22 |
| 323.15 | 35080.00 | 722.75 |
| 323.15 | 40050.00 | 726.09 |
| 323.15 | 45060.00 | 729.27 |
| 323.15 | 50030.00 | 732.36 |
| 323.15 | 55050.00 | 735.35 |
| 323.15 | 60010.00 | 738.19 |
| 323.15 | 65010.00 | 741.02 |
| 323.15 | 5060.00 | 699.09 |
| 348.15 | 1010.00 | 675.18 |
| 348.15 | 5040.00 | 679.76 |
| 348.15 | 10030.00 | 685.0 |
| 348.15 | 15020.00 | 689.84 |
| 348.15 | 20040.00 | 694.44 |
| 348.15 | 25050.00 | 698.79 |
| 348.15 | 30030.00 | 702.84 |
| 348.15 | 35050.00 | 706.74 |
| 348.15 | 40020.00 | 710.4 |
| 348.15 | 45070.00 | 714.01 |
| 348.15 | 50040.00 | 717.37 |
| 348.15 | 55050.00 | 720.67 |
| 348.15 | 60000.00 | 723.79 |
| 348.15 | 65040.00 | 726.84 |
| 348.15 | 5030.00 | 679.76 |
| 373.15 | 1010.00 | 654.52 |
| 373.15 | 5050.00 | 659.99 |
| 373.15 | 10030.00 | 666.13 |
| 373.15 | 15070.00 | 671.78 |
| 373.15 | 20030.00 | 677.04 |
| 373.15 | 25060.00 | 681.94 |
| 373.15 | 30040.00 | 686.51 |
| 373.15 | 35060.00 | 690.83 |
| 373.15 | 40020.00 | 694.95 |
| 373.15 | 45070.00 | 698.87 |
| 373.15 | 50070.00 | 702.65 |
| 373.15 | 55060.00 | 706.23 |
| 373.15 | 60040.00 | 709.66 |
| 373.15 | 65030.00 | 712.95 |
| 373.15 | 5050.00 | 659.99 |
| 398.15 | 1020.00 | 633.06 |
| 398.15 | 5020.00 | 639.53 |
| 398.15 | 10050.00 | 646.89 |
| 398.15 | 15070.00 | 653.53 |
| 398.15 | 20020.00 | 659.49 |
| 398.15 | 25030.00 | 665.05 |
| 398.15 | 30050.00 | 670.22 |
| 398.15 | 35050.00 | 675.1 |
| 398.15 | 40020.00 | 679.63 |
| 398.15 | 45070.00 | 683.97 |
| 398.15 | 50020.00 | 688.07 |
| 398.15 | 55040.00 | 692.01 |
| 398.15 | 60030.00 | 695.72 |
| 398.15 | 65040.00 | 699.37 |
| 398.15 | 5030.00 | 639.58 |
| 423.15 | 1020.00 | 610.45 |
| 423.15 | 5030.00 | 618.42 |
| 423.15 | 10030.00 | 627.15 |
| 423.15 | 15030.00 | 634.86 |
| 423.15 | 20040.00 | 641.8 |
| 423.15 | 25040.00 | 648.1 |
| 423.15 | 30020.00 | 653.92 |
| 423.15 | 35050.00 | 659.35 |
| 423.15 | 40020.00 | 664.4 |
| 423.15 | 45020.00 | 669.15 |
| 423.15 | 50040.00 | 673.7 |
| 423.15 | 55020.00 | 677.97 |
| 423.15 | 60030.00 | 682.03 |
| 423.15 | 65040.00 | 685.95 |
| 423.15 | 5030.00 | 618.47 |
| 448.15 | 1000.00 | 586.37 |
| 448.15 | 5020.00 | 596.41 |
| 448.15 | 10040.00 | 607.05 |
| 448.15 | 15010.00 | 616.06 |
| 448.15 | 20010.00 | 624.0 |
| 448.15 | 25040.00 | 631.27 |
| 448.15 | 30030.00 | 637.78 |
| 448.15 | 35030.00 | 643.8 |
| 448.15 | 40010.00 | 649.38 |
| 448.15 | 45050.00 | 654.67 |
| 448.15 | 50020.00 | 659.58 |
| 448.15 | 55040.00 | 664.24 |
| 448.15 | 60030.00 | 668.62 |
| 448.15 | 65020.00 | 672.85 |
| 448.15 | 5020.00 | 596.46 |
| 473.15 | 5010.00 | 573.14 |
| 473.15 | 10040.00 | 586.15 |
| 473.15 | 15040.00 | 596.86 |
| 473.15 | 20020.00 | 606.05 |
| 473.15 | 25050.00 | 614.28 |
| 473.15 | 30020.00 | 621.6 |
| 473.15 | 35030.00 | 628.3 |
| 473.15 | 40050.00 | 634.51 |
| 473.15 | 45050.00 | 640.25 |
| 473.15 | 50040.00 | 645.6 |
| 473.15 | 55020.00 | 650.62 |
| 473.15 | 60010.00 | 655.39 |
| 473.15 | 65010.00 | 659.92 |
| 473.15 | 5010.00 | 573.14 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 293.21 | 1993.00 | 719.36 |
| 293.21 | 3991.00 | 721.16 |
| 293.21 | 5993.00 | 722.88 |
| 293.21 | 7996.00 | 724.42 |
| 293.21 | 10001.00 | 725.92 |
| 293.21 | 13001.00 | 728.0 |
| 293.22 | 16000.00 | 730.02 |
| 293.21 | 19004.00 | 732.11 |
| 293.21 | 22005.00 | 734.14 |
| 293.21 | 24997.00 | 736.13 |
| 293.21 | 27997.00 | 738.31 |
| 293.21 | 29995.00 | 739.58 |
| 313.11 | 2000.00 | 704.08 |
| 313.11 | 4007.00 | 705.88 |
| 313.11 | 6006.00 | 707.62 |
| 313.11 | 8004.00 | 709.24 |
| 313.11 | 10007.00 | 710.92 |
| 313.11 | 13003.00 | 713.28 |
| 313.11 | 16007.00 | 715.76 |
| 313.10 | 19007.00 | 718.18 |
| 313.10 | 22007.00 | 720.52 |
| 313.10 | 25009.00 | 722.7 |
| 313.10 | 28007.00 | 724.82 |
| 313.10 | 30010.00 | 726.21 |
| 333.00 | 2014.00 | 688.53 |
| 333.00 | 3990.00 | 690.6 |
| 333.00 | 5995.00 | 692.58 |
| 333.01 | 8001.00 | 694.51 |
| 333.01 | 10007.00 | 696.11 |
| 333.01 | 13004.00 | 698.84 |
| 333.01 | 16002.00 | 701.48 |
| 333.01 | 19006.00 | 704.03 |
| 333.01 | 22003.00 | 706.5 |
| 333.01 | 25006.00 | 708.9 |
| 333.01 | 28003.00 | 711.23 |
| 333.01 | 30012.00 | 712.74 |
| 353.12 | 2004.00 | 672.27 |
| 353.12 | 3995.00 | 674.59 |
| 353.12 | 6000.00 | 676.83 |
| 353.12 | 8005.00 | 679.1 |
| 353.12 | 10010.00 | 681.31 |
| 353.12 | 13002.00 | 684.37 |
| 353.12 | 16003.00 | 687.3 |
| 353.12 | 18999.00 | 689.99 |
| 353.12 | 22002.00 | 692.72 |
| 353.12 | 25004.00 | 695.35 |
| 353.12 | 28007.00 | 697.9 |
| 353.12 | 30003.00 | 699.56 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 100.00 | 283.15 | 725.6 |
| 100.00 | 288.15 | 721.6 |
| 100.00 | 293.15 | 717.8 |
| 100.00 | 298.15 | 713.7 |
| 100.00 | 303.15 | 709.9 |
| 100.00 | 308.15 | 706.0 |
| 100.00 | 313.15 | 701.9 |
| 100.00 | 318.15 | 698.1 |
| 100.00 | 323.15 | 694.1 |
| 3000.00 | 283.15 | 727.7 |
| 3000.00 | 288.15 | 723.8 |
| 3000.00 | 293.15 | 720.0 |
| 3000.00 | 298.15 | 716.1 |
| 3000.00 | 303.15 | 712.3 |
| 3000.00 | 308.15 | 708.5 |
| 3000.00 | 313.15 | 704.5 |
| 3000.00 | 318.15 | 700.7 |
| 3000.00 | 323.15 | 696.9 |
| 5000.00 | 283.15 | 729.1 |
| 5000.00 | 288.15 | 725.3 |
| 5000.00 | 293.15 | 721.5 |
| 5000.00 | 298.15 | 717.7 |
| 5000.00 | 303.15 | 713.9 |
| 5000.00 | 308.15 | 710.1 |
| 5000.00 | 313.15 | 706.3 |
| 5000.00 | 318.15 | 702.4 |
| 5000.00 | 323.15 | 698.6 |
| 7500.00 | 283.15 | 730.8 |
| 7500.00 | 288.15 | 727.0 |
| 7500.00 | 293.15 | 723.4 |
| 7500.00 | 298.15 | 719.5 |
| 7500.00 | 303.15 | 715.8 |
| 7500.00 | 308.15 | 712.1 |
| 7500.00 | 313.15 | 708.3 |
| 7500.00 | 318.15 | 704.6 |
| 7500.00 | 323.15 | 700.8 |
| 10000.00 | 283.15 | 732.6 |
| 10000.00 | 288.15 | 728.9 |
| 10000.00 | 293.15 | 725.2 |
| 10000.00 | 298.15 | 721.5 |
| 10000.00 | 303.15 | 717.8 |
| 10000.00 | 308.15 | 714.2 |
| 10000.00 | 313.15 | 710.4 |
| 10000.00 | 318.15 | 706.8 |
| 10000.00 | 323.15 | 703.0 |
| 20000.00 | 283.15 | 739.2 |
| 20000.00 | 288.15 | 735.7 |
| 20000.00 | 293.15 | 732.2 |
| 20000.00 | 298.15 | 728.7 |
| 20000.00 | 303.15 | 725.2 |
| 20000.00 | 308.15 | 721.7 |
| 20000.00 | 313.15 | 718.2 |
| 20000.00 | 318.15 | 714.7 |
| 20000.00 | 323.15 | 711.2 |
| 30000.00 | 283.15 | 745.3 |
| 30000.00 | 288.15 | 742.0 |
| 30000.00 | 293.15 | 738.7 |
| 30000.00 | 298.15 | 735.2 |
| 30000.00 | 303.15 | 731.9 |
| 30000.00 | 308.15 | 728.5 |
| 30000.00 | 313.15 | 725.3 |
| 30000.00 | 318.15 | 721.9 |
| 30000.00 | 323.15 | 718.6 |
| 40000.00 | 283.15 | 751.1 |
| 40000.00 | 288.15 | 747.9 |
| 40000.00 | 293.15 | 744.6 |
| 40000.00 | 298.15 | 741.4 |
| 40000.00 | 303.15 | 738.2 |
| 40000.00 | 308.15 | 735.0 |
| 40000.00 | 313.15 | 731.8 |
| 40000.00 | 318.15 | 728.6 |
| 40000.00 | 323.15 | 725.4 |
| 50000.00 | 283.15 | 756.4 |
| 50000.00 | 288.15 | 753.4 |
| 50000.00 | 293.15 | 750.3 |
| 50000.00 | 298.15 | 747.1 |
| 50000.00 | 303.15 | 744.1 |
| 50000.00 | 308.15 | 740.9 |
| 50000.00 | 313.15 | 737.8 |
| 50000.00 | 318.15 | 734.8 |
| 50000.00 | 323.15 | 731.6 |
| 60000.00 | 283.15 | 761.6 |
| 60000.00 | 288.15 | 758.5 |
| 60000.00 | 293.15 | 755.5 |
| 60000.00 | 298.15 | 752.5 |
| 60000.00 | 303.15 | 749.5 |
| 60000.00 | 308.15 | 746.6 |
| 60000.00 | 313.15 | 743.5 |
| 60000.00 | 318.15 | 740.5 |
| 60000.00 | 323.15 | 737.5 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Speed of sound, m/s - Liquid |
| 100.00 | 293.15 | 1226.379 |
| 100.00 | 313.15 | 1146.226 |
| 100.00 | 333.15 | 1068.198 |
| 100.00 | 353.15 | 992.6189 |
| 100.00 | 373.15 | 922.1599 |
| 100.00 | 393.15 | 867.4314 |
| 10000.00 | 293.15 | 1288.02 |
| 10000.00 | 313.15 | 1212.824 |
| 10000.00 | 333.15 | 1140.94 |
| 10000.00 | 353.15 | 1072.568 |
| 10000.00 | 373.15 | 1004.987 |
| 10000.00 | 393.15 | 946.865 |
| 20000.00 | 293.15 | 1344.821 |
| 20000.00 | 313.15 | 1274.241 |
| 20000.00 | 333.15 | 1206.915 |
| 20000.00 | 353.15 | 1142.609 |
| 20000.00 | 373.15 | 1081.282 |
| 20000.00 | 393.15 | 1022.924 |
| 30000.00 | 293.15 | 1396.854 |
| 30000.00 | 313.15 | 1329.834 |
| 30000.00 | 333.15 | 1266.203 |
| 30000.00 | 353.15 | 1205.597 |
| 30000.00 | 373.15 | 1148.091 |
| 30000.00 | 393.15 | 1093.674 |
| 40000.00 | 293.15 | 1445.084 |
| 40000.00 | 313.15 | 1380.943 |
| 40000.00 | 353.15 | 1262.461 |
| 40000.00 | 373.15 | 1207.979 |
| 40000.00 | 393.15 | 1156.595 |
| 50000.00 | 293.15 | 1490.057 |
| 50000.00 | 313.15 | 1428.288 |
| 50000.00 | 333.15 | 1369.835 |
| 50000.00 | 353.15 | 1314.591 |
| 50000.00 | 373.15 | 1262.528 |
| 50000.00 | 393.15 | 1213.59 |
| 60000.00 | 293.15 | 1532.464 |
| 60000.00 | 313.15 | 1472.742 |
| 60000.00 | 333.15 | 1416.313 |
| 60000.00 | 353.15 | 1363.169 |
| 60000.00 | 373.15 | 1313.133 |
| 60000.00 | 393.15 | 1266.136 |
| 70000.00 | 293.15 | 1572.512 |
| 70000.00 | 313.15 | 1514.719 |
| 70000.00 | 333.15 | 1460.059 |
| 70000.00 | 353.15 | 1408.501 |
| 70000.00 | 373.15 | 1360.053 |
| 70000.00 | 393.15 | 1314.71 |
| 80000.00 | 293.15 | 1610.591 |
| 80000.00 | 313.15 | 1554.351 |
| 80000.00 | 333.15 | 1501.308 |
| 80000.00 | 353.15 | 1451.316 |
| 80000.00 | 373.15 | 1404.349 |
| 80000.00 | 393.15 | 1360.387 |
| 90000.00 | 293.15 | 1646.928 |
| 90000.00 | 313.15 | 1592.049 |
| 90000.00 | 333.15 | 1540.349 |
| 90000.00 | 353.15 | 1491.697 |
| 90000.00 | 373.15 | 1446.071 |
| 90000.00 | 393.15 | 1403.307 |
| 100000.00 | 293.15 | 1681.563 |
| 100000.00 | 313.15 | 1628.026 |
| 100000.00 | 333.15 | 1577.369 |
| 100000.00 | 353.15 | 1529.841 |
| 100000.00 | 373.15 | 1485.463 |
| 100000.00 | 393.15 | 1443.653 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [310.51; 451.94] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.45385e+01 | |||
| Coefficient B | -3.70195e+03 | |||
| Coefficient C | -5.07360e+01 | |||
| Temperature range, min. | 310.51 | |||
| Temperature range, max. | 451.94 | |||
|
T(K) Vapor pressure (kPa) 0 50 100 150 200 350 400 450 | ||||
| Pvap | 1.33 | kPa | 310.51 | Calculated Property |
| Pvap | 3.01 | kPa | 326.22 | Calculated Property |
| Pvap | 6.21 | kPa | 341.94 | Calculated Property |
| Pvap | 11.90 | kPa | 357.65 | Calculated Property |
| Pvap | 21.42 | kPa | 373.37 | Calculated Property |
| Pvap | 36.50 | kPa | 389.08 | Calculated Property |
| Pvap | 59.31 | kPa | 404.80 | Calculated Property |
| Pvap | 92.49 | kPa | 420.51 | Calculated Property |
| Pvap | 139.11 | kPa | 436.23 | Calculated Property |
| Pvap | 202.64 | kPa | 451.94 | Calculated Property |
| Pvap | [6.08e-04; 2266.69] | kPa | [219.63; 595.65] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 7.25466e+01 | |||
| Coefficient B | -7.73941e+03 | |||
| Coefficient C | -8.32740e+00 | |||
| Coefficient D | 3.89483e-06 | |||
| Temperature range, min. | 219.63 | |||
| Temperature range, max. | 595.65 | |||
|
T(K) Vapor pressure (kPa) 0 500 1000 1500 2000 300 400 500 600 | ||||
| Pvap | 6.08e-04 | kPa | 219.63 | Calculated Property |
| Pvap | 0.04 | kPa | 261.41 | Calculated Property |
| Pvap | 0.81 | kPa | 303.19 | Calculated Property |
| Pvap | 6.78 | kPa | 344.97 | Calculated Property |
| Pvap | 33.28 | kPa | 386.75 | Calculated Property |
| Pvap | 113.80 | kPa | 428.53 | Calculated Property |
| Pvap | 301.98 | kPa | 470.31 | Calculated Property |
| Pvap | 667.88 | kPa | 512.09 | Calculated Property |
| Pvap | 1292.71 | kPa | 553.87 | Calculated Property |
| Pvap | 2266.69 | kPa | 595.65 | Calculated Property |
Similar Compounds
Find more compounds similar to Nonane.
Mixtures
- 1-Hexanol + Nonane
- o-Toluidine + Nonane
- Benzene + Nonane
- 2-Propanol, 2-methyl- + Nonane
- Nonane + Cyclohexane
- Toluene + Nonane
- Benzene, 1,3-dimethyl- + Nonane
- p-Xylene + Nonane
- Heptane + Nonane
- Methyl formate + Nonane
- Ethyl formate + Nonane
- Formic acid, propyl ester + Nonane
- Formic acid, butyl ester + Nonane
- Carbon dioxide + Nonane
- Fluoroform + Nonane
- Ethane, hexafluoro- + Nonane
- Acetic acid, methyl ester + Nonane
- Ethyl Acetate + Nonane
- n-Propyl acetate + Nonane
- Acetic acid, butyl ester + Nonane
Find more mixtures with Nonane.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Speed-of-Sound Measurements in n-Nonane at Temperatures between 293.15 and 393.15 K and at Pressures up to 100 MPa
- Determination of excess molar enthalpies of the ternary system methyl tert-butyl ether + 1-pentanol + nonane at 298.15K Analysis and comparison with predicted values of the UNIFAC model and some empirical methods
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- High pressure vapor liquid equilibria for the systems thiophene + nonane +CO2, and thiophene + decane +CO2
- Density and surface tension variation with temperature for n-nonane + 1-hexanol
- Liquid liquid equilibrium of (perfluoroalkane + alkane) binary mixtures
- Infinite dilution activity coefficients, specific retention volumes and solvation thermodynamics of hydrocarbons in C78H158 branched alkane solvent
- Measurement of infinite dilution activity coefficients of n-alkanes in 4-methyl-n-butylpyridinium tetrafluoroborate using gas liquid chromatography
- Thermodynamics of mixtures containing amines VI. Liquid liquid equilibria for mixtures of o-toluidine + selected alkanes
- New isothermal vapor liquid equilibria for the CO2 + n-nonane, and CO2 + n-undecane systems
- Measurement of vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1-alkyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide and prediction of these properties and A using modified UNIFAC (Dortmund)
- Liquid liquid equilibrium of ternary systems 1-butyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic
- Measurement and prediction of activity coefficients at infinite dilution ( ), vapor.liquid equilibria (VLE) and excess enthalpies (HE) of binary systems with 1,1-dialkyl-pyrrolidinium bis(trifluoromethylsulfonyl)imide using mod. UNIFAC (Dortmund)
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium trifluoromethanesulfonate using GLC
- (Solid + liquid) and (liquid + liquid) phase equilibria measurements and correlation of the binary systems {tri-iso-butyl(methyl)phosphonium tosylate + alcohol, or +hydrocarbon}
- Activity coefficients at infinite dilution of alkanes and alkenes in 1-alkyl-3-methylimidazolium tetrafluoroborate
- Activity coefficients at infinite dilution measurements for organic solutes and water in the 1-hexyloxymethyl-3-methyl-imidazolium and 1,3-dihexyloxymethyl-imidazolium bis(trifluoromethylsulfonyl)-imide ionic liquids The cation influence
- Vapor liquid equilibria and density measurement for binary mixtures of toluene, benzene, o-xylene, m-xylene, sulfolane and nonane at 333.15K and 353.15K
- Liquid liquid equilibrium of ternary systems 1-octyl-3-methylimidazolium hexafluorophosphate + aromatic + aliphatic hydrocarbons
- Gas-liquid chromatography measurements of activity coefficients at infinite dilution of hydrocarbons and alkanols in 1-alkyl-3-methylimidazolium bis(oxalato)borate
- Viscosity of the binary systems 2-methyl-2-propanol with n-alkanes at T = (303.15, 308.15, 313.15, 318.15 and 323.15) K: Prediction and correlation - New UNIFAC-VISCO interaction parameters
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- Introduction of the amine group at cycloaliphatic hydrocarbon (c-CHNH2) for the modified UNIFAC (Dortmund) model and validation in multicomponent systems containing cyclohexylamine
- Isobaric vapor-liquid equilibrium for the binary mixtures of nonane with cyclohexane, toluene, m-xylene, or p-xylene at 101.3 kPa
- Liquid-liquid equilibria of mixtures with ethyl lactate and various hydrocarbons
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Distribution of MEG and methanol in well-defined hydrocarbon and water systems: Experimental measurement and modeling using the CPA EoS
- Vapor liquid equilibrium for the ternary carbon dioxide ethanol nonane and decane systems
- Liquid-liquid equilibria containing fluorous solvents as environmentally benign solvent
- Isobaric vapor-liquid equilibrium for binary systemsof toluene + o-xylene, benzene + o-xylene, nonane + benzene and nonane + heptane at 101.3 kPa
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Solutions of alkyl methanoates and alkanes: Simultaneous modeling of phase equilibria and mixing properties. Estimation of behavior by UNIFAC with recalculation of parameters
- Activity coefficients at infinite dilution of organic solvents and water in 1-butyl-3-methylimidazolium dicyanamide. A literature review of hexane/hex-1-ene separation
- 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
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- 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)
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- 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
- Physical properties of {anisole + n-alkanes} at temperatures between (293.15 and 303.15) K
- Thermodynamic properties of (an ester + and alkane). XVII. Experimental He and Ve values for (an alkyl propanoate + an alkane) at 318.15K
- Coexistence curves of critical nonaqueous microemulsions of (AOT + DMA + nonane) and (AOT + DMA + octane)
- Excess properties of the binary mixtures of methylcyclohexane + alkanes (C6 to C12) at T = 298.15 K to T = 308.15 K
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- (p,Vm,T) measurements of (cyclohexane + nonane) at temperatures from 298.15 K to 328.15 K and at pressures up to 40 MPa
- Measurements of activity coefficients at infinite dilution of aromatic and aliphatic hydrocarbons, alcohols, and water in the new ionic liquid [EMIM][SCN] using GLC
- Measurement and correlation of the (p, ?, T) relation of liquid n-heptane, n-nonane, 2,4-dichlorotoluene, and bromobenzene in the temperature range from (233.15 to 473.15) K at pressures up to 30 MPa for use as density reference liquids
- 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 measurements for organic solutes and water in the ionic liquid triethylsulphonium bis(trifluoromethylsulfonyl)imide
- Measurements of activity coefficients at infinite dilution of aliphatic and aromatic hydrocarbons, alcohols, thiophene, tetrahydrofuran, MTBE, and water in ionic liquid [BMIM][SCN] using GLC
- Experimental densities, refractive indices, and speeds of sound of 12 binary mixtures containing alkanes and aromatic compounds at T = 313.15 K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Separation of benzene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at several temperatures and atmospheric pressure: Effect of the size of the aliphatic hydrocarbons
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- LLE data for the ionic liquid 3-methyl-N-butyl pyridinium dicyanamide with several aromatic and aliphatic hydrocarbons
- Gas liquid chromatography measurements of activity coefficients at infinite dilution of various organic solutes and water in tri-iso-butylmethylphosphonium tosylate ionic liquid
- Separation of toluene from alkanes using 1-ethyl-3-methylpyridinium ethylsulfate ionic liquid at T = 298.15 K and atmospheric pressure
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate [EMIM][TCB] using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of organic solutes and water in 1-propyl-1-methylpiperidinium bis{(trifluoromethyl)sulfonyl}imide ionic liquid using g.l.c.
- Activity coefficients at infinite dilution of organic solutes in N-alkylpyridinium bis(trifluoromethylsulfonyl)imide ([CnPY][NTf2], n = 2, 4, 5) using gas liquid chromatography
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- Extraction of toluene from aliphatic compounds using an ionic liquid as solvent: Influence of the alkane on the (liquid + liquid) equilibrium
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyl(tetradecyl)phosphonium tetrafluoroborate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 373.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium hexafluoroantimonate using gas liquid chromatography at T = (313.15, 323.15, and 333.15) K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid, methyl(trioctyl)ammonium thiosalicylate, [N1888][TS] by gas liquid chromatography at T = (303.15, 313.15, and 323.15) K
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(3-hydroxypropyl)pyridinium bis(trifluoromethylsulfonyl)-amide
- Thermodynamics and activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tetracyanoborate
- (Liquid + liquid) equilibrium for binary systems of N-formylmorpholine with alkanes
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium hexafluorophosphate using gas liquid chromatography at T = (313.15, 333.15, 353.15, and 363.15) K
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpiperidinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Experimental and theoretical study on infinite dilution activity coefficients of various solutes in piperidinium ionic liquids
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Activity coefficients at infinite dilution of organic solutes in N-formylmorpholine and N-methylpyrrolidone from gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-hydroxyethyl)- 3-methylimidazolium trifluorotris(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of organic solutes in diethylene glycol and triethylene glycol from gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- Evaluation of ionic liquids as solvent for aromatic extraction: Experimental, correlation and COSMO-RS predictions
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Density, viscosity and excess molar volume of binary mixtures of tri-n-octylamine + diluents (n-heptane, n-octane, n-nonane, and n-decane) at various temperatures
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium 2-(2-methoxyethoxy) ethylsulfate at T = (308.15, 313.15, 323.15 and 333.15) K using gas + liquid chromatography
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- (Liquid + liquid) equilibrium at T = 298.15 K for ternary mixtures of alkane + aromatic compounds + imidazolium-based ionic liquids
- Excess molar enthalpies for binary mixtures of cyclopentanone, cyclohexanone, or cycloheptanone with n-nonane at T = 298.15 K and atmospheric pressure
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Thermodynamics of solvation in propylene glycol and methyl cellosolve
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Activity coefficients at infinite dilution, physicochemical and thermodynamic properties for organic solutes and water in the ionic liquid ethyl-dimethyl-(2-methoxyethyl)ammonium trifluorotris-(perfluoroethyl)phosphate
- Activity coefficients at infinite dilution of alkanes, alkenes, alkyl benzenes in dimethylphosphate based ionic liquids using gas liquid chromatography
- Screening of environmental friendly ionic liquid as a solvent for the different types of separations problem: Insight from activity coefficients at infinite dilution measurement using (gas + liquid) chromatography technique
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Experimental determination of critical data of multi-component mixtures containing potential gasoline additives 2-butanol by a flow-type apparatus
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in 1-allyl-3-methylimidazolium bis{(trifluoromethyl)sulfonyl}imide ionic liquid
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Activity coefficients at infinite dilution of hydrocarbons in glycols: Experimental data and thermodynamic modeling with the GCA-EoS
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Pressure dependence of the solubility of light fullerenes in n-nonane
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Experiment and correlation of the equilibrium interfacial tension for paraffin + CO2 modified with ethanol
- Thermodynamics of mixtures containing aromatic nitriles
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Density, sound speed and derived thermophysical properties of n-nonane at temperatures between (283.15 and 473.15)K and at pressures up to 390MPa
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Liquid-liquid equilibria for (2-hydroxy benzaldehyde + n-alkane) mixtures. Intermolecular and proximity effects in systems containing hydroxyl and aldehyde groups
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- Thermodynamic behaviour of the binary systems dimethyl carbonate + n-octane or n-nonane
- Bubble Point Measurements of n-Butane + n-Octane and n-Butane + n-Nonane Binary Mixtures
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Densities and Viscosities of Corn Oil + n-Alkanes Blends from (288.15 to 343.15) K at 0.1 MPa
- 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
- Simultaneous Measurement of Dynamic Viscosity and Density of n-Alkanes at High Pressures
- Vapor-Liquid Equilibrium Measurements of Ethanol and n-Nonane or n-Decane Binary Mixtures with Large Relative Volatility
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- P-rho-T Data and Modeling for Propan-1-ol + n-Octane or n-Nonane or n-Decane from 313.15 K to 363.15 K and 1 MPa to 20 MPa
- Measurement of Critical Properties for Binary and Ternary Mixtures Containing n-Butanol and n-Alkane
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Liquid Extraction of Toluene from Heptane, Octane, or Nonane Using Mixed Ionic Solvents of 1-Ethyl-3-methylimidazolium Methylsulfate and 1-Hexyl-3-methylimidazolium Hexafluorophosphate
- Low-Pressure VLE Measurements and Thermodynamic Modeling, with PSRK and NRTL, of Binary 1-Alcohol + n-Alkane Systems
- Measuring Activity Coefficient at Infinite Dilution of Hydrocarbons in Ionic Liquids and Evaluation of Other Thermodynamic Properties using Gas Chromatography
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Infinite Dilution Activity Coefficients of Hydrocarbons in Triethylene Glycol and Tetraethylene Glycol
- Densities and Excess Molar Properties of Dimethyl Carbonate with Alkanes (C6 to C10) and VLE of Dimethyl Carbonate with Alkanes (C9 to C10) at 101.3 kPa
- Vapor-Liquid Equilibrium Studies for Systems Containing n-Butylisocyanate at Temperatures between 323.15 K and 371.15 K
- Solubility of Benzophenone in Binary Alkane + Carbon Tetrachloride Solvent Mixtures
- Liquid-Liquid Equilibria of Methyl Acetate + Methanol + Octane or Nonane
- Liquid-Liquid Equilibria for Monoethylene Glycol + Water + Alkane Systems in the Range (273 to 313) K and Atmospheric Pressure
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + Nonane + Cyclohexanol
- 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
- Surface Properties of Dilute Solutions of Alkanes in Benzyl Alcohol
- Isobaric Vapor-Liquid Equilibria of the Ternary System Methylbutyl Ketone + 1-Pentanol + Nonane
- 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
- Thermodynamics of Mixtures Containing a Strongly Polar Compound. 8. Liquid-Liquid Equilibria for N,N-Dialkylamide + Selected N-Alkanes
- 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
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Isobaric Vapor-Liquid Equilibria of the Ternary System Dibutyl Ether + 1-Pentanol + Nonane
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Measurements of Density and Heat Capacity for Binary Mixtures {x Benzonitrile + (1 -x) (Octane or Nonane)}
- Separation of Benzene from Linear Alkanes (C6-C9) Using 1-Ethyl-3-Methylimidazolium Ethylsulfate at T = 298.15 K
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Vapor-Liquid Equilibria and Density Measurement for Binary Mixtures of Benzene + Nonane, Methylbenzene + 1,2-Dimethylbenzene, 1,3-Dimethylbenzene + 2,3,4,5-Tetrahydrothiophene-1,1-dioxide (Sulfolane), 1,2-Dimethylbenzene + Sulfolane, 1,2-Dimethylbenzene + N-Methylformamide (NMF), 1,3-Dimethylbenzene + NMF, and 1,4-Dimethylbenzene + NMF from (333.15 to 353.15) K at Vacuum Conditions
- Liquid-Liquid Equilibria of the Ternary Systems of Alkane + Aromatic + 1-Ethylpyridinium Ethylsulfate Ionic Liquid at T = (283.15 and 298.15) K
- Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Decyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Isobaric Vapor-Liquid Equilibria of the Ternary System Pentan-1-ol + Pentyl Acetate + Nonane
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Ethyl-3-methylimidazolium Diethylphosphate Using Gas Liquid Chromatography
- Apparent and Partial Molar Volumes at Infinite Dilution and Solid Liquid Equilibria of Dibenzothiophene + Alkane Systems
- Experimental Liquid Densities of n-Pentane, n-Octane, and n-Nonane and Their Binary Mixtures from (273.15 to 363.15) K at 0.1 MPa
- Vapor Liquid Equilibria of Binary and Ternary Systems Containing Carbon Dioxide, Alkane, and Benzothiophene
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Density, Refractive Index, Viscosity, and Surface Tension of Binary Mixtures of exo-Tetrahydrodicyclopentadiene with Some n-Alkanes from (293.15 to 313.15) K
- Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-Methylpropane, Ethanol, and Nonane
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Dibutylphosphate Using Gas Liquid Chromatography
- 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
- Measurements and Correlations of the Isobaric Vapor Liquid Equilibria of Binary Mixtures and Excess Properties for Mixtures Containing an Alkyl (Methyl, Ethyl) Butanoate with an Alkane (Heptane, Nonane) at 101.3 kPa
- Densities, Viscosities, and Refractive Indices of Binary Mixtures of 1,2,3,4-Tetrahydronaphthalene with Some n-Alkanes at T = (293.15 to 313.15) K
- Multiproperty Correlation of Experimental Data of the Binaries Propyl Ethanoate + Alkanes (Pentane to Decane). New Experimental Information for Vapor Liquid Equilibrium and Mixing Properties
- 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
- 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
- Improvements in the Experimentation and the Representation of Thermodynamic Properties (iso-p VLE and yE) of Alkyl Propanoate + Alkane Binaries
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Liquid Liquid Extraction of Toluene from n-Alkanes using {[4empy][Tf2N] + [emim][DCA]} Ionic Liquid Mixtures
- Comparison Study on Temperature Dependence of the Interfacial Tension of n-Alkane Water and n-Alcohol Water Two Binary Systems
- Vapor Liquid Equilibria Measurements for the Nine n-Alkane/Ketone Pairs Comprising 2-, 3-, and 4-Heptanone with n-Octane, n-Nonane, and n-Decane
- Determination of the Critical Properties of C6 C10 n-Alkanes and Their Binary Systems Using a Flow Apparatus
- Measurement of the Critical Properties of the Ternary Systems Hexane + Heptane + Octane and Octane + Nonane + Decane Using a Flow Apparatus
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Temperature Dependence of the Speed of Sound of Nonane + 1-Chlorononane in the Range of (293.15 to 423.15) K
- Measurement of Activity Coefficient at Infinite Dilution of Hydrocarbons in Sulfolane Using Gas-Liquid Chromatography
- Densities and Viscosities of Ternary Mixtures of Heptane, Octane, Nonane, and Hexyl Benzene from 293.15 K to 313.15 K
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Densities and Viscosities of MTBE + Nonane or Decane at p = 0.1 MPa from (273.15 to 363.15) K
- Isobaric Vapor Liquid Equilibria of the Ternary System 1-Pentanol + Nonane Anisole
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-Hexyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Surface Tension of Dilute Solutions of Alkanes in Cyclohexanol at Different Temperatures
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- 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
- Excess Molar Enthalpies of Ternary and Binary Mixtures Containing 2-Methoxy-2-methylpropane, 1-Propanol, and Nonane
- Paramagnetic Ionic Liquid 1-Butyl-3-methylimidazolium Tetrabromidocobaltate(II): Activity Coefficients at Infinite Dilution of Organic Solutes and Crystal Structure
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Phase Equilibria of (1-Hexyl-3-methylimidazolium Thiocyanate + Water, Alcohol, or Hydrocarbon) Binary Systems
- Activity Coefficients at Infinite Dilution of Alkanes, Alkenes, and Alkyl Benzenes in Glycerol Using Gas-Liquid Chromatography
- Thermodynamics of Mixtures Containing a Strongly Polar Compound. 9. Liquid-Liquid Equilibria for epsilon-Caprolactam + Selected Alkanes
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tris(pentafluoroethyl)trifluorophosphate [EMIM][FAP] Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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