- InChI
- InChI=1S/C3H6O/c1-3(2)4/h1-2H3
- InChI Key
- CSCPPACGZOOCGX-UHFFFAOYSA-N
- Formula
- C3H6O
- SMILES
- CC(C)=O
- Molecular Weight1
- 58.08
- CAS
- 67-64-1
- Other Names
-
- (CH3)2CO
- 2-propanone
- Chevron acetone
- Dimethylformaldehyde
- Dimethylketal
- Ketone propane
- Ketone, dimethyl-
- Methyl ketone
- NSC 135802
- Rcra waste number U002
- Sasetone
- UN 1090
- dimethyl ketone
- propan-2-one
- propanone
- pyroacetic ether
- «beta»-Ketopropane
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (kJ/mol).
- ΔcH°gas : Standard gas enthalpy of combustion (kJ/mol).
- 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).
- Cp,solid : Solid phase heat capacity (J/mol×K).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- Tflash,oc : Flash Point (Open Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- 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).
- 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.
- NFPA Health : NFPA Health 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.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (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).
- Tboilr : Boiling point at reduced pressure (K).
- Tc : Critical Temperature (K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Pressure Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3040 | KDB | |
| PAff | [811.50; 815.20] | kJ/mol |
|
| PAff | 812.00 | kJ/mol | NIST |
| PAff | 815.20 | kJ/mol | NIST |
| PAff | 814.30 | kJ/mol | NIST |
| PAff | 812.60 ± 0.20 | kJ/mol | NIST |
| PAff | 811.50 ± 3.40 | kJ/mol | NIST |
| PAff | 811.50 ± 3.40 | kJ/mol | NIST |
| Tig | 738.15 | K | KDB |
| BasG | [782.00; 784.70] | kJ/mol |
|
| BasG | 782.10 | kJ/mol | NIST |
| BasG | Outlier 784.70 | kJ/mol | NIST |
| BasG | 782.20 | kJ/mol | NIST |
| BasG | 782.00 ± 0.20 | kJ/mol | NIST |
| BasG | 782.10 ± 1.50 | kJ/mol | NIST |
| BasG | 782.10 ± 1.50 | kJ/mol | NIST |
| ΔcH°gas | -1821.40 ± 0.84 | kJ/mol | NIST |
| ΔcH°liquid | [-1804.20; -1772.00] | kJ/mol |
|
| ΔcH°liquid | -1772.00 | kJ/mol | NIST |
| ΔcH°liquid | -1804.20 | kJ/mol | NIST |
| μ | 2.90 | debye | KDB |
| η | [0.0003000; 0.0003121] | Pa×s |
|
| η | 0.0003121 | Pa×s | Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents |
| η | 0.0003000 | Pa×s | Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures |
| EA | 0.00 | eV | NIST |
| LFL | 2.60 | % in Air | KDB |
| UFL | 12.80 | % in Air | KDB |
| Tflash,cc | 257.59 | K | KDB |
| Tflash,oc | 255.37 | K | KDB |
| ΔfG° | -153.20 | kJ/mol | KDB |
| Rg | 2.7400 | KDB | |
| ΔfH°gas | [-218.50; -216.40] | kJ/mol |
|
| ΔfH°gas | -217.70 | kJ/mol | KDB |
| ΔfH°gas | -218.50 ± 0.59 | kJ/mol | NIST |
| ΔfH°gas | -217.10 ± 0.50 | kJ/mol | NIST |
| ΔfH°gas | -217.50 ± 0.67 | kJ/mol | NIST |
| ΔfH°gas | -216.40 | kJ/mol | NIST |
| ΔfH°liquid | -249.40 ± 0.63 | kJ/mol | NIST |
| ΔfusH° | 5.12 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [29.70; 31.30] | kJ/mol |
|
| ΔvapH° | 31.27 | kJ/mol | NIST |
| ΔvapH° | 31.30 | kJ/mol | NIST |
| ΔvapH° | 29.70 ± 0.00 | kJ/mol | NIST |
| IE | [9.50; 9.80] | eV |
|
| IE | 9.70 ± 0.01 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.69 ± 0.01 | eV | NIST |
| IE | 9.68 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.71 ± 0.03 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.70 ± 0.00 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.75 ± 0.03 | eV | NIST |
| IE | 9.72 | eV | NIST |
| IE | 9.74 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.74 ± 0.03 | eV | NIST |
| IE | 9.68 | eV | NIST |
| IE | 9.71 ± 0.01 | eV | NIST |
| IE | 9.70 ± 0.10 | eV | NIST |
| IE | 9.68 ± 0.02 | eV | NIST |
| IE | 9.67 | eV | NIST |
| IE | 9.71 ± 0.03 | eV | NIST |
| IE | 9.71 ± 0.03 | eV | NIST |
| IE | 9.69 ± 0.01 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | Outlier 9.80 | eV | NIST |
| IE | 9.72 | eV | NIST |
| IE | 9.68 | eV | NIST |
| IE | 9.71 ± 0.02 | eV | NIST |
| IE | Outlier 9.50 | eV | NIST |
| IE | 9.70 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.71 | eV | NIST |
| IE | 9.72 | eV | NIST |
| log10WS | 0.57 | Relay (1.0) Calculated Property | |
| logPoct/wat | 0.595 | Crippen Calculated Property | |
| McVol | 54.700 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 1 | KDB | |
| Pc | [4700.00; 5290.00] | kPa |
|
| Pc | 4700.00 | kPa | KDB |
| Pc | 4700.00 ± 10.00 | kPa | NIST |
| Pc | 4700.00 ± 6.00 | kPa | NIST |
| Pc | 4758.22 ± 10.13 | kPa | NIST |
| Pc | 5062.20 ± 50.66 | kPa | NIST |
| Pc | 4700.00 ± 101.32 | kPa | NIST |
| Pc | 4790.00 ± 34.50 | kPa | NIST |
| Pc | 4720.00 ± 101.32 | kPa | NIST |
| Pc | 4740.00 ± 405.30 | kPa | NIST |
| Pc | Outlier 5290.00 ± 405.30 | kPa | NIST |
| ρc | [234.06; 278.20] | kg/m3 |
|
| ρc | 268.91 ± 2.90 | kg/m3 | NIST |
| ρc | 234.06 ± 1.51 | kg/m3 | NIST |
| ρc | 278.20 ± 9.87 | kg/m3 | NIST |
| ρc | 272.97 ± 1.16 | kg/m3 | NIST |
| ρc | 252.06 ± 1.74 | kg/m3 | NIST |
| Inp | [437.00; 512.00] |
|
|
| Inp | 470.23 | NIST | |
| Inp | 470.90 | NIST | |
| Inp | 470.70 | NIST | |
| Inp | 470.10 | NIST | |
| Inp | 469.67 | NIST | |
| Inp | 469.50 | NIST | |
| Inp | 469.28 | NIST | |
| Inp | 469.41 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 469.00 | NIST | |
| Inp | 469.00 | NIST | |
| Inp | 481.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 477.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 488.70 | NIST | |
| Inp | 488.20 | NIST | |
| Inp | 485.00 | NIST | |
| Inp | 497.00 | NIST | |
| Inp | 475.00 | NIST | |
| Inp | Outlier 437.00 | NIST | |
| Inp | Outlier 437.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 443.50 | NIST | |
| Inp | 465.00 | NIST | |
| Inp | 441.00 | NIST | |
| Inp | 444.00 | NIST | |
| Inp | Outlier 439.00 | NIST | |
| Inp | 459.00 | NIST | |
| Inp | 443.00 | NIST | |
| Inp | 472.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 475.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 447.00 | NIST | |
| Inp | Outlier 439.00 | NIST | |
| Inp | 503.00 | NIST | |
| Inp | 477.55 | NIST | |
| Inp | Outlier 510.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 503.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 475.30 | NIST | |
| Inp | 481.00 | NIST | |
| Inp | 481.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 488.60 | NIST | |
| Inp | 471.00 | NIST | |
| Inp | 474.00 | NIST | |
| Inp | 468.00 | NIST | |
| Inp | 466.00 | NIST | |
| Inp | 471.00 | NIST | |
| Inp | 480.00 | NIST | |
| Inp | 472.00 | NIST | |
| Inp | 473.00 | NIST | |
| Inp | 472.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 466.00 | NIST | |
| Inp | 468.00 | NIST | |
| Inp | 466.00 | NIST | |
| Inp | 479.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 496.00 | NIST | |
| Inp | 496.00 | NIST | |
| Inp | 472.00 | NIST | |
| Inp | 502.00 | NIST | |
| Inp | 502.00 | NIST | |
| Inp | 487.00 | NIST | |
| Inp | 476.60 | NIST | |
| Inp | 503.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 487.00 | NIST | |
| Inp | 474.00 | NIST | |
| Inp | 474.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 509.00 | NIST | |
| Inp | Outlier 512.00 | NIST | |
| Inp | 459.00 | NIST | |
| Inp | 471.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 476.00 | NIST | |
| Inp | 501.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 497.00 | NIST | |
| Inp | 472.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 460.00 | NIST | |
| Inp | 473.00 | NIST | |
| Inp | 473.00 | NIST | |
| Inp | 473.00 | NIST | |
| Inp | 465.00 | NIST | |
| Inp | 460.00 | NIST | |
| Inp | 469.00 | NIST | |
| Inp | 491.00 | NIST | |
| Inp | 474.00 | NIST | |
| Inp | 484.00 | NIST | |
| Inp | 468.00 | NIST | |
| Inp | 469.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 503.00 | NIST | |
| Inp | 500.00 | NIST | |
| Inp | 470.23 | NIST | |
| Inp | 469.50 | NIST | |
| Inp | 469.00 | NIST | |
| Inp | 478.00 | NIST | |
| Inp | 475.00 | NIST | |
| Inp | 465.00 | NIST | |
| Inp | 443.00 | NIST | |
| Inp | 447.00 | NIST | |
| Inp | 479.00 | NIST | |
| Inp | 502.00 | NIST | |
| Inp | 477.55 | NIST | |
| Inp | 468.00 | NIST | |
| Inp | 471.00 | NIST | |
| Inp | 470.00 | NIST | |
| I | [775.00; 854.00] |
|
|
| I | 843.50 | NIST | |
| I | 835.00 | NIST | |
| I | 837.50 | NIST | |
| I | 840.80 | NIST | |
| I | 832.00 | NIST | |
| I | Outlier 847.00 | NIST | |
| I | Outlier 785.00 | NIST | |
| I | 842.00 | NIST | |
| I | 824.00 | NIST | |
| I | 821.00 | NIST | |
| I | 813.00 | NIST | |
| I | 814.00 | NIST | |
| I | 814.00 | NIST | |
| I | 814.00 | NIST | |
| I | 820.00 | NIST | |
| I | 818.00 | NIST | |
| I | 794.00 | NIST | |
| I | 809.00 | NIST | |
| I | 813.00 | NIST | |
| I | 834.00 | NIST | |
| I | 842.00 | NIST | |
| I | 814.00 | NIST | |
| I | 821.30 | NIST | |
| I | 814.00 | NIST | |
| I | 802.00 | NIST | |
| I | 813.00 | NIST | |
| I | 818.00 | NIST | |
| I | 811.00 | NIST | |
| I | 816.00 | NIST | |
| I | 822.00 | NIST | |
| I | 813.00 | NIST | |
| I | 814.00 | NIST | |
| I | 819.00 | NIST | |
| I | 813.00 | NIST | |
| I | 812.00 | NIST | |
| I | 830.00 | NIST | |
| I | 808.00 | NIST | |
| I | 808.00 | NIST | |
| I | 834.00 | NIST | |
| I | 832.00 | NIST | |
| I | 841.00 | NIST | |
| I | 821.00 | NIST | |
| I | 812.00 | NIST | |
| I | 811.00 | NIST | |
| I | 823.00 | NIST | |
| I | 820.00 | NIST | |
| I | 810.00 | NIST | |
| I | 827.00 | NIST | |
| I | 827.00 | NIST | |
| I | 828.00 | NIST | |
| I | 825.00 | NIST | |
| I | 811.00 | NIST | |
| I | 816.00 | NIST | |
| I | 820.00 | NIST | |
| I | 816.00 | NIST | |
| I | 832.00 | NIST | |
| I | 814.00 | NIST | |
| I | 845.00 | NIST | |
| I | 798.00 | NIST | |
| I | 825.00 | NIST | |
| I | 814.00 | NIST | |
| I | 823.00 | NIST | |
| I | 821.00 | NIST | |
| I | 846.00 | NIST | |
| I | 805.00 | NIST | |
| I | 820.00 | NIST | |
| I | 810.00 | NIST | |
| I | 810.00 | NIST | |
| I | 822.00 | NIST | |
| I | 810.00 | NIST | |
| I | 822.00 | NIST | |
| I | Outlier 854.00 | NIST | |
| I | 816.00 | NIST | |
| I | 800.00 | NIST | |
| I | 818.00 | NIST | |
| I | 845.00 | NIST | |
| I | 814.00 | NIST | |
| I | 814.00 | NIST | |
| I | Outlier 775.00 | NIST | |
| I | 821.00 | NIST | |
| I | 841.00 | NIST | |
| I | 836.00 | NIST | |
| I | 816.00 | NIST | |
| I | 813.00 | NIST | |
| I | 815.00 | NIST | |
| I | 814.00 | NIST | |
| I | 819.00 | NIST | |
| I | Outlier 788.00 | NIST | |
| I | 823.00 | NIST | |
| I | Outlier 847.00 | NIST | |
| I | 835.00 | NIST | |
| I | 810.00 | NIST | |
| I | 824.00 | NIST | |
| I | 815.00 | NIST | |
| I | 820.00 | NIST | |
| I | 821.00 | NIST | |
| I | 820.00 | NIST | |
| I | 816.00 | NIST | |
| I | 810.00 | NIST | |
| I | Outlier 847.00 | NIST | |
| I | 819.00 | NIST | |
| I | 810.00 | NIST | |
| I | 813.00 | NIST | |
| I | 830.00 | NIST | |
| I | 809.00 | NIST | |
| I | 821.30 | NIST | |
| I | 811.00 | NIST | |
| I | 794.00 | NIST | |
| S°liquid | [200.00; 220.50] | J/mol×K |
|
| S°liquid | 200.40 | J/mol×K | NIST |
| S°liquid | 200.00 | J/mol×K | NIST |
| S°liquid | 220.50 | J/mol×K | NIST |
| S°liquid | 217.60 | J/mol×K | NIST |
| Tboil | [323.40; 331.15] | K |
|
| Tboil | 329.30 | K | Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone |
| Tboil | 329.26 | K | Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa |
| Tboil | 329.56 | K | Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone) |
| Tboil | 329.33 | K | Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation |
| Tboil | 329.35 | K | Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide |
| Tboil | 329.27 | K | Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K |
| Tboil | 329.37 | K | Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa |
| Tboil | 329.20 | K | KDB |
| Tboil | 329.20 ± 0.20 | K | NIST |
| Tboil | 329.30 ± 0.20 | K | NIST |
| Tboil | 329.45 ± 0.15 | K | NIST |
| Tboil | 329.45 ± 0.30 | K | NIST |
| Tboil | 329.00 | K | NIST |
| Tboil | 329.21 ± 0.04 | K | NIST |
| Tboil | 329.30 | K | NIST |
| Tboil | 329.45 ± 0.30 | K | NIST |
| Tboil | 329.40 ± 0.40 | K | NIST |
| Tboil | 329.25 ± 0.30 | K | NIST |
| Tboil | 329.47 ± 0.50 | K | NIST |
| Tboil | 329.23 ± 0.05 | K | NIST |
| Tboil | 329.25 ± 0.05 | K | NIST |
| Tboil | 329.26 ± 0.30 | K | NIST |
| Tboil | 329.00 ± 0.20 | K | NIST |
| Tboil | 329.30 ± 0.20 | K | NIST |
| Tboil | 329.30 ± 0.06 | K | NIST |
| Tboil | 329.25 | K | NIST |
| Tboil | 329.25 ± 0.15 | K | NIST |
| Tboil | 329.38 ± 0.30 | K | NIST |
| Tboil | 329.40 ± 0.20 | K | NIST |
| Tboil | 329.15 ± 0.30 | K | NIST |
| Tboil | 329.00 ± 1.00 | K | NIST |
| Tboil | 329.30 ± 0.20 | K | NIST |
| Tboil | 329.30 ± 0.30 | K | NIST |
| Tboil | 329.40 ± 0.40 | K | NIST |
| Tboil | 329.25 ± 0.50 | K | NIST |
| Tboil | 329.25 ± 0.30 | K | NIST |
| Tboil | 329.21 ± 0.10 | K | NIST |
| Tboil | 329.25 ± 0.30 | K | NIST |
| Tboil | 329.26 ± 0.30 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | Outlier 330.95 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 0.50 | K | NIST |
| Tboil | 329.26 ± 0.50 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | Outlier 326.15 ± 1.00 | K | NIST |
| Tboil | 329.33 ± 0.20 | K | NIST |
| Tboil | 329.25 ± 1.00 | K | NIST |
| Tboil | 329.75 ± 1.00 | K | NIST |
| Tboil | 328.90 ± 0.40 | K | NIST |
| Tboil | 329.25 ± 0.50 | K | NIST |
| Tboil | 329.35 ± 1.00 | K | NIST |
| Tboil | 329.28 ± 0.15 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 0.50 | K | NIST |
| Tboil | 329.35 ± 0.50 | K | NIST |
| Tboil | 329.35 ± 0.50 | K | NIST |
| Tboil | 329.35 ± 0.50 | K | NIST |
| Tboil | 329.35 ± 0.20 | K | NIST |
| Tboil | 329.33 ± 0.20 | K | NIST |
| Tboil | 329.28 ± 0.30 | K | NIST |
| Tboil | 329.50 ± 0.50 | K | NIST |
| Tboil | 329.30 ± 0.50 | K | NIST |
| Tboil | 329.65 ± 0.50 | K | NIST |
| Tboil | 328.65 ± 1.00 | K | NIST |
| Tboil | 329.35 ± 0.50 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.30 ± 0.50 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | Outlier 323.40 ± 0.30 | K | NIST |
| Tboil | 329.27 ± 0.50 | K | NIST |
| Tboil | 329.30 ± 0.50 | K | NIST |
| Tboil | 329.40 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 1.00 | K | NIST |
| Tboil | 330.15 ± 0.50 | K | NIST |
| Tboil | 329.75 ± 0.50 | K | NIST |
| Tboil | 329.25 ± 1.00 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.20 ± 1.00 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | 329.26 ± 0.10 | K | NIST |
| Tboil | Outlier 331.15 ± 3.00 | K | NIST |
| Tboil | 328.85 ± 1.00 | K | NIST |
| Tboil | 329.15 ± 2.00 | K | NIST |
| Tboil | 328.57 ± 1.00 | K | NIST |
| Tboil | 329.30 ± 1.00 | K | NIST |
| Tboil | 329.55 ± 1.00 | K | NIST |
| Tboil | 329.65 ± 0.30 | K | NIST |
| Tboil | 328.75 ± 1.00 | K | NIST |
| Tboil | 328.95 ± 1.00 | K | NIST |
| Tboil | 329.40 ± 0.20 | K | NIST |
| Tboil | 329.39 ± 0.50 | K | NIST |
| Tboil | 330.00 ± 1.00 | K | NIST |
| Tboil | 329.35 ± 0.30 | K | NIST |
| Tboil | 329.35 ± 0.30 | K | NIST |
| Tboil | 329.45 ± 1.00 | K | NIST |
| Tboil | 329.35 ± 0.30 | K | NIST |
| Tboil | 329.25 ± 0.20 | K | NIST |
| Tboil | 329.30 ± 0.40 | K | NIST |
| Tboil | 329.35 ± 0.20 | K | NIST |
| Tboil | 329.17 ± 0.20 | K | NIST |
| Tboil | 329.50 ± 0.50 | K | NIST |
| Tboil | 329.32 ± 0.30 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | 329.35 ± 1.00 | K | NIST |
| Tboil | 329.22 ± 0.20 | K | NIST |
| Tboil | 329.23 ± 0.10 | K | NIST |
| Tboil | 329.30 ± 1.00 | K | NIST |
| Tboil | 329.20 ± 0.30 | K | NIST |
| Tboil | 329.48 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 1.00 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.35 ± 1.00 | K | NIST |
| Tboil | 329.45 ± 0.50 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.30 ± 0.30 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | 329.65 ± 1.00 | K | NIST |
| Tboil | 329.70 ± 1.50 | K | NIST |
| Tboil | 329.30 ± 0.50 | K | NIST |
| Tboil | 329.40 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 0.30 | K | NIST |
| Tboil | 329.30 ± 0.50 | K | NIST |
| Tboil | 329.30 ± 1.00 | K | NIST |
| Tboil | 329.25 ± 0.30 | K | NIST |
| Tboil | 330.20 ± 1.00 | K | NIST |
| Tboil | 329.34 ± 0.50 | K | NIST |
| Tboil | 329.15 ± 1.00 | K | NIST |
| Tboil | 329.40 ± 1.00 | K | NIST |
| Tboil | 329.55 ± 1.00 | K | NIST |
| Tboil | 330.15 ± 1.00 | K | NIST |
| Tboil | 329.55 ± 1.00 | K | NIST |
| Tboil | 328.90 ± 1.00 | K | NIST |
| Tboil | 329.50 ± 1.00 | K | NIST |
| Tboil | 329.50 ± 0.50 | K | NIST |
| Tboil | Outlier 330.85 ± 1.00 | K | NIST |
| Tboil | 329.45 ± 1.00 | K | NIST |
| Tboil | 329.45 ± 1.00 | K | NIST |
| Tc | [505.80; 509.40] | K |
|
| Tc | 508.10 | K | KDB |
| Tc | 508.20 | K | NIST |
| Tc | 508.35 ± 0.40 | K | NIST |
| Tc | 508.10 ± 0.20 | K | NIST |
| Tc | 508.10 ± 0.06 | K | NIST |
| Tc | 508.70 ± 0.70 | K | NIST |
| Tc | 508.20 ± 0.40 | K | NIST |
| Tc | 509.10 ± 0.80 | K | NIST |
| Tc | 508.15 ± 0.20 | K | NIST |
| Tc | 508.15 ± 0.50 | K | NIST |
| Tc | 507.70 ± 1.00 | K | NIST |
| Tc | 509.40 ± 0.39 | K | NIST |
| Tc | 508.10 ± 0.25 | K | NIST |
| Tc | 508.70 ± 1.00 | K | NIST |
| Tc | 509.00 ± 1.00 | K | NIST |
| Tc | 508.75 ± 0.30 | K | NIST |
| Tc | 506.90 ± 1.00 | K | NIST |
| Tc | 507.60 ± 1.00 | K | NIST |
| Tc | Outlier 505.80 ± 2.00 | K | NIST |
| Tc | Outlier 506.00 ± 2.00 | K | NIST |
| Tfus | [177.80; 179.37] | K |
|
| Tfus | 178.30 | K | KDB |
| Tfus | 179.00 | K | NIST |
| Tfus | 178.45 | K | NIST |
| Tfus | 178.25 ± 0.10 | K | NIST |
| Tfus | 178.10 ± 0.10 | K | NIST |
| Tfus | 178.55 ± 0.05 | K | NIST |
| Tfus | 177.80 ± 0.20 | K | NIST |
| Tfus | 179.37 ± 0.50 | K | NIST |
| Tfus | 178.60 ± 0.20 | K | NIST |
| Tfus | 179.15 ± 0.30 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Tfus | 178.85 ± 0.30 | K | NIST |
| Tfus | 179.00 ± 2.00 | K | NIST |
| Ttriple | [176.60; 178.50] | K |
|
| Ttriple | 178.50 ± 0.30 | K | NIST |
| Ttriple | 176.60 ± 0.15 | K | NIST |
| Ttriple | 177.60 ± 0.30 | K | NIST |
| Ttriple | 177.60 ± 0.20 | K | NIST |
| Ttriple | 176.60 ± 0.15 | K | NIST |
| Ttriple | 177.60 ± 0.30 | K | NIST |
| Ttriple | 177.60 ± 0.20 | K | NIST |
| Vc | 0.209 | m3/kmol | KDB |
| Zc | 0.2325190 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboilr | 329.30 | K | 2.70 | NIST |
Datasets
Viscosity, Pa*s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Viscosity, Pa*s - Liquid |
| 303.15 | 101.30 | 0.0003 |
| Reference | ||
Speed of sound, m/s
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 265.67 | 102.00 | 1298.93 |
| 265.67 | 504.00 | 1301.09 |
| 265.67 | 750.00 | 1302.5 |
| 265.67 | 1003.00 | 1303.56 |
| 265.67 | 1255.00 | 1304.92 |
| 265.67 | 1501.00 | 1306.29 |
| 265.67 | 2007.00 | 1308.73 |
| 265.67 | 2506.00 | 1311.28 |
| 265.67 | 3005.00 | 1313.79 |
| 265.67 | 4004.00 | 1318.59 |
| 265.67 | 5004.00 | 1323.31 |
| 265.67 | 6005.00 | 1328.01 |
| 265.67 | 8002.00 | 1338.69 |
| 265.67 | 10001.00 | 1349.81 |
| 265.67 | 12001.00 | 1358.7 |
| 265.67 | 14003.00 | 1366.48 |
| 265.67 | 16050.00 | 1375.48 |
| 265.67 | 18001.00 | 1384.77 |
| 265.67 | 20003.00 | 1394.13 |
| 265.67 | 23001.00 | 1407.08 |
| 265.67 | 27004.00 | 1425.32 |
| 265.67 | 31003.00 | 1439.78 |
| 265.67 | 34997.00 | 1455.17 |
| 265.67 | 39999.00 | 1476.05 |
| 265.67 | 45002.00 | 1494.61 |
| 265.67 | 49999.00 | 1511.6 |
| 265.67 | 55001.00 | 1528.77 |
| 265.67 | 60002.00 | 1548.05 |
| 265.67 | 65000.00 | 1564.17 |
| 265.67 | 18001.00 | 1384.54 |
| 273.16 | 102.00 | 1264.48 |
| 273.16 | 504.00 | 1266.57 |
| 273.16 | 750.00 | 1267.96 |
| 273.16 | 1003.00 | 1269.39 |
| 273.16 | 1255.00 | 1270.74 |
| 273.16 | 1501.00 | 1272.23 |
| 273.16 | 2007.00 | 1275.12 |
| 273.16 | 2506.00 | 1277.93 |
| 273.16 | 3005.00 | 1281.1 |
| 273.16 | 4004.00 | 1287.23 |
| 273.16 | 5004.00 | 1291.97 |
| 273.16 | 6005.00 | 1296.6 |
| 273.16 | 8002.00 | 1306.58 |
| 273.16 | 10001.00 | 1316.19 |
| 273.16 | 12001.00 | 1325.58 |
| 273.16 | 14003.00 | 1335.9 |
| 273.16 | 16005.00 | 1346.87 |
| 273.16 | 18001.00 | 1355.99 |
| 273.16 | 20003.00 | 1363.63 |
| 273.16 | 23001.00 | 1376.52 |
| 273.16 | 27004.00 | 1394.61 |
| 273.16 | 31003.00 | 1412.24 |
| 273.16 | 34997.00 | 1428.86 |
| 273.16 | 39999.00 | 1446.67 |
| 273.16 | 45002.00 | 1467.44 |
| 273.16 | 49999.00 | 1485.84 |
| 273.16 | 55001.00 | 1504.31 |
| 273.16 | 60002.00 | 1520.08 |
| 273.16 | 65000.00 | 1538.71 |
| 273.16 | 3005.00 | 1281.19 |
| 273.16 | 4004.00 | 1286.78 |
| 273.16 | 5004.00 | 1292.02 |
| 280.74 | 75.00 | 1233.63 |
| 280.74 | 504.00 | 1234.94 |
| 280.74 | 750.00 | 1236.39 |
| 280.74 | 1003.00 | 1237.85 |
| 280.74 | 1255.00 | 1239.22 |
| 280.74 | 1501.00 | 1240.59 |
| 280.74 | 2007.00 | 1243.75 |
| 280.74 | 2506.00 | 1247.03 |
| 280.74 | 3005.00 | 1249.76 |
| 280.74 | 4004.00 | 1255.13 |
| 280.74 | 5004.00 | 1259.87 |
| 280.74 | 6005.00 | 1264.8 |
| 280.74 | 8002.00 | 1275.79 |
| 280.74 | 10001.00 | 1286.82 |
| 280.74 | 12001.00 | 1296.79 |
| 280.74 | 14003.00 | 1306.71 |
| 280.74 | 16005.00 | 1316.23 |
| 280.74 | 18001.00 | 1325.46 |
| 280.74 | 20003.00 | 1335.09 |
| 280.74 | 23001.00 | 1350.8 |
| 280.74 | 27004.00 | 1366.99 |
| 280.74 | 31003.00 | 1384.26 |
| 280.74 | 34997.00 | 1401.32 |
| 280.74 | 39999.00 | 1423.56 |
| 280.74 | 45002.00 | 1441.37 |
| 280.74 | 49999.00 | 1461.28 |
| 280.74 | 55001.00 | 1480.44 |
| 280.74 | 60002.00 | 1498.97 |
| 280.74 | 65000.00 | 1514.56 |
| 280.74 | 75.00 | 1232.04 |
| 280.74 | 23001.00 | 1350.8 |
| 280.74 | 39999.00 | 1423.74 |
| 280.74 | 45002.00 | 1441.37 |
| 280.74 | 60002.00 | 1498.91 |
| 280.74 | 65000.00 | 1514.63 |
| 288.23 | 109.00 | 1199.01 |
| 288.23 | 504.00 | 1201.24 |
| 288.23 | 750.00 | 1202.57 |
| 288.23 | 1003.00 | 1204.2 |
| 288.23 | 1255.00 | 1205.54 |
| 288.23 | 1501.00 | 1206.97 |
| 288.23 | 2007.00 | 1209.92 |
| 288.23 | 2506.00 | 1212.8 |
| 288.23 | 3005.00 | 1215.61 |
| 288.23 | 4004.00 | 1221.35 |
| 288.23 | 5004.00 | 1227.14 |
| 288.23 | 6005.00 | 1232.71 |
| 288.23 | 8002.00 | 1244.39 |
| 288.23 | 10001.00 | 1255.4 |
| 288.23 | 12001.00 | 1265.22 |
| 288.23 | 14003.00 | 1275.63 |
| 288.23 | 16005.00 | 1286.61 |
| 288.23 | 18001.00 | 1296.18 |
| 288.23 | 20003.00 | 1305.89 |
| 288.23 | 23001.00 | 1319.61 |
| 288.23 | 27004.00 | 1339.05 |
| 288.23 | 31003.00 | 1357.37 |
| 288.23 | 34997.00 | 1373.83 |
| 288.23 | 39999.00 | 1395.08 |
| 288.23 | 45002.00 | 1416.1 |
| 288.23 | 49999.00 | 1435.37 |
| 288.23 | 55001.00 | 1453.97 |
| 288.23 | 60002.00 | 1473.72 |
| 288.23 | 65000.00 | 1492.08 |
| 298.23 | 109.00 | 1153.69 |
| 298.23 | 504.00 | 1156.23 |
| 298.23 | 750.00 | 1157.82 |
| 298.23 | 1003.00 | 1159.5 |
| 298.23 | 1255.00 | 1161.14 |
| 298.23 | 1501.00 | 1162.71 |
| 298.23 | 2007.00 | 1165.65 |
| 298.23 | 2506.00 | 1168.6 |
| 298.23 | 3005.00 | 1171.49 |
| 298.23 | 4004.00 | 1177.4 |
| 298.23 | 5004.00 | 1182.9 |
| 298.23 | 6005.00 | 1189.6 |
| 298.23 | 8002.00 | 1201.45 |
| 298.23 | 10001.00 | 1212.8 |
| 298.23 | 12001.00 | 1223.83 |
| 298.23 | 14003.00 | 1234.83 |
| 298.23 | 16005.00 | 1246.18 |
| 298.23 | 18001.00 | 1256.46 |
| 298.23 | 20003.00 | 1265.92 |
| 298.23 | 23001.00 | 1281.93 |
| 298.23 | 27004.00 | 1301.17 |
| 298.23 | 31003.00 | 1319.28 |
| 298.23 | 34997.00 | 1337.9 |
| 298.23 | 39999.00 | 1359.25 |
| 298.23 | 45002.00 | 1380.44 |
| 298.23 | 49999.00 | 1400.61 |
| 298.23 | 55001.00 | 1421.32 |
| 298.23 | 60002.00 | 1439.68 |
| 298.23 | 65000.00 | 1458.59 |
| 308.22 | 109.00 | 1107.74 |
| 308.22 | 504.00 | 1110.52 |
| 308.22 | 750.00 | 1112.35 |
| 308.22 | 1003.00 | 1114.01 |
| 308.22 | 1255.00 | 1115.75 |
| 308.22 | 1501.00 | 1117.34 |
| 308.22 | 2007.00 | 1120.69 |
| 308.22 | 2506.00 | 1123.91 |
| 308.22 | 3005.00 | 1127.11 |
| 308.22 | 4004.00 | 1133.79 |
| 308.22 | 5004.00 | 1140.56 |
| 308.22 | 6005.00 | 1146.98 |
| 308.22 | 8002.00 | 1159.51 |
| 308.22 | 10001.00 | 1171.13 |
| 308.22 | 12001.00 | 1182.37 |
| 308.22 | 14003.00 | 1194.75 |
| 308.22 | 16005.00 | 1205.76 |
| 308.22 | 18001.00 | 1216.57 |
| 308.22 | 20003.00 | 1227.49 |
| 308.22 | 23001.00 | 1244.05 |
| 308.22 | 27004.00 | 1263.44 |
| 308.22 | 31003.00 | 1283.97 |
| 308.22 | 34997.00 | 1302.46 |
| 308.22 | 39999.00 | 1324.45 |
| 308.22 | 45002.00 | 1347.09 |
| 308.22 | 49999.00 | 1367.79 |
| 308.22 | 55001.00 | 1388.31 |
| 308.22 | 60002.00 | 1408.07 |
| 308.22 | 65000.00 | 1427.73 |
| 318.22 | 109.00 | 1062.32 |
| 318.22 | 504.00 | 1065.38 |
| 318.22 | 750.00 | 1067.34 |
| 318.22 | 1003.00 | 1069.21 |
| 318.22 | 1255.00 | 1071.11 |
| 318.22 | 1501.00 | 1072.72 |
| 318.22 | 2007.00 | 1076.32 |
| 318.22 | 2506.00 | 1079.71 |
| 318.22 | 3005.00 | 1083.5 |
| 318.22 | 4004.00 | 1090.38 |
| 318.22 | 5004.00 | 1096.85 |
| 318.22 | 6005.00 | 1103.61 |
| 318.22 | 8002.00 | 1116.61 |
| 318.22 | 10001.00 | 1129.13 |
| 318.22 | 12001.00 | 1142.47 |
| 318.22 | 14003.00 | 1154.62 |
| 318.22 | 16005.00 | 1166.43 |
| 318.22 | 18001.00 | 1177.61 |
| 318.22 | 20003.00 | 1189.14 |
| 318.22 | 23001.00 | 1205.63 |
| 318.22 | 27004.00 | 1226.77 |
| 318.22 | 31003.00 | 1247.41 |
| 318.22 | 34997.00 | 1266.28 |
| 318.22 | 39999.00 | 1290.76 |
| 318.22 | 45002.00 | 1313.78 |
| 318.22 | 49999.00 | 1334.83 |
| 318.22 | 55001.00 | 1356.46 |
| 318.22 | 60002.00 | 1376.77 |
| 318.22 | 65000.00 | 1395.43 |
| 328.22 | 129.00 | 1018.3 |
| 328.22 | 504.00 | 1021.14 |
| 328.22 | 750.00 | 1023.1 |
| 328.22 | 1003.00 | 1024.91 |
| 328.22 | 1255.00 | 1026.82 |
| 328.22 | 1501.00 | 1028.6 |
| 328.22 | 2007.00 | 1032.33 |
| 328.22 | 2506.00 | 1036.21 |
| 328.22 | 3005.00 | 1040.05 |
| 328.22 | 4004.00 | 1047.07 |
| 328.22 | 5004.00 | 1053.76 |
| 328.22 | 6005.00 | 1060.7 |
| 328.22 | 8002.00 | 1074.73 |
| 328.22 | 10001.00 | 1088.42 |
| 328.22 | 12001.00 | 1101.14 |
| 328.22 | 14003.00 | 1113.97 |
| 328.22 | 16005.00 | 1126.49 |
| 328.22 | 18001.00 | 1138.92 |
| 328.22 | 20003.00 | 1151.08 |
| 328.22 | 23001.00 | 1168.1 |
| 328.22 | 27004.00 | 1190.45 |
| 328.22 | 31003.00 | 1211.66 |
| 328.22 | 34997.00 | 1231.66 |
| 328.22 | 39999.00 | 1256.67 |
| 328.22 | 45002.00 | 1280.63 |
| 328.22 | 49999.00 | 1303.34 |
| 328.22 | 55001.00 | 1324.67 |
| 328.22 | 60002.00 | 1345.81 |
| 328.22 | 65000.00 | 1365.57 |
| 338.22 | 170.00 | 972.8 |
| 338.22 | 504.00 | 976.32 |
| 338.22 | 750.00 | 978.88 |
| 338.22 | 1003.00 | 981.05 |
| 338.22 | 1255.00 | 982.97 |
| 338.22 | 1501.00 | 984.75 |
| 338.22 | 2007.00 | 988.42 |
| 338.22 | 2506.00 | 992.07 |
| 338.22 | 3005.00 | 996.0 |
| 338.22 | 4004.00 | 1004.26 |
| 338.22 | 5004.00 | 1011.63 |
| 338.22 | 6005.00 | 1019.16 |
| 338.22 | 8002.00 | 1033.34 |
| 338.22 | 10001.00 | 1047.72 |
| 338.22 | 12001.00 | 1061.19 |
| 338.22 | 14003.00 | 1074.71 |
| 338.22 | 16005.00 | 1088.09 |
| 338.22 | 18001.00 | 1100.33 |
| 338.22 | 20003.00 | 1112.58 |
| 338.22 | 23001.00 | 1131.02 |
| 338.22 | 27004.00 | 1154.76 |
| 338.22 | 31003.00 | 1176.19 |
| 338.22 | 34997.00 | 1197.57 |
| 338.22 | 39999.00 | 1223.29 |
| 338.22 | 45002.00 | 1248.14 |
| 338.22 | 49999.00 | 1271.19 |
| 338.22 | 55001.00 | 1293.31 |
| 338.22 | 60002.00 | 1315.39 |
| 338.22 | 65000.00 | 1336.38 |
| Reference | ||
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Speed of sound, m/s - Liquid |
| 248.15 | 100.00 | 1390.16 |
| 248.15 | 10000.00 | 1435.51 |
| 248.15 | 20000.00 | 1478.36 |
| 248.15 | 30000.00 | 1518.03 |
| 248.15 | 40000.00 | 1550.78 |
| 248.15 | 50000.00 | 1590.88 |
| 248.15 | 60000.00 | 1625.12 |
| 248.15 | 70000.00 | 1657.38 |
| 248.15 | 80000.00 | 1688.07 |
| 248.15 | 90000.00 | 1717.48 |
| 248.15 | 100000.00 | 1745.43 |
| 253.15 | 100.00 | 1367.16 |
| 253.15 | 10000.00 | 1413.84 |
| 253.15 | 20000.00 | 1457.41 |
| 253.15 | 30000.00 | 1497.98 |
| 253.15 | 40000.00 | 1536.44 |
| 253.15 | 50000.00 | 1572.26 |
| 253.15 | 60000.00 | 1606.9 |
| 253.15 | 70000.00 | 1639.52 |
| 253.15 | 80000.00 | 1670.88 |
| 253.15 | 90000.00 | 1700.93 |
| 253.15 | 100000.00 | 1729.65 |
| 258.15 | 100.00 | 1344.2 |
| 258.15 | 10000.00 | 1391.98 |
| 258.15 | 20000.00 | 1436.58 |
| 258.15 | 30000.00 | 1478.11 |
| 258.15 | 40000.00 | 1517.33 |
| 258.15 | 50000.00 | 1553.89 |
| 258.15 | 60000.00 | 1588.88 |
| 258.15 | 70000.00 | 1621.91 |
| 258.15 | 80000.00 | 1653.89 |
| 258.15 | 90000.00 | 1684.43 |
| 258.15 | 100000.00 | 1713.62 |
| 263.15 | 100.00 | 1320.92 |
| 263.15 | 10000.00 | 1370.35 |
| 263.15 | 20000.00 | 1415.99 |
| 263.15 | 30000.00 | 1458.25 |
| 263.15 | 40000.00 | 1498.44 |
| 263.15 | 50000.00 | 1535.81 |
| 263.15 | 60000.00 | 1570.98 |
| 263.15 | 70000.00 | 1604.54 |
| 263.15 | 80000.00 | 1637.11 |
| 263.15 | 90000.00 | 1668.1 |
| 263.15 | 100000.00 | 1697.74 |
| 268.15 | 100.00 | 1298.67 |
| 268.15 | 10000.00 | 1349.08 |
| 268.15 | 20000.00 | 1395.62 |
| 268.15 | 30000.00 | 1438.54 |
| 268.15 | 40000.00 | 1479.77 |
| 268.15 | 50000.00 | 1517.83 |
| 268.15 | 60000.00 | 1553.2 |
| 268.15 | 70000.00 | 1587.43 |
| 268.15 | 80000.00 | 1620.54 |
| 268.15 | 90000.00 | 1651.96 |
| 268.15 | 100000.00 | 1682.01 |
| 273.15 | 100.00 | 1275.4 |
| 273.15 | 10000.00 | 1327.81 |
| 273.15 | 20000.00 | 1375.45 |
| 273.15 | 30000.00 | 1418.96 |
| 273.15 | 40000.00 | 1461.31 |
| 273.15 | 50000.00 | 1499.98 |
| 273.15 | 60000.00 | 1535.77 |
| 273.15 | 70000.00 | 1570.58 |
| 273.15 | 80000.00 | 1604.15 |
| 273.15 | 90000.00 | 1636.02 |
| 273.15 | 100000.00 | 1666.45 |
| 278.15 | 100.00 | 1253.32 |
| 278.15 | 10000.00 | 1306.75 |
| 278.15 | 20000.00 | 1355.49 |
| 278.15 | 30000.00 | 1400.47 |
| 278.15 | 40000.00 | 1443.03 |
| 278.15 | 50000.00 | 1481.78 |
| 278.15 | 60000.00 | 1518.62 |
| 278.15 | 70000.00 | 1553.98 |
| 278.15 | 80000.00 | 1587.94 |
| 278.15 | 90000.00 | 1620.26 |
| 278.15 | 100000.00 | 1650.92 |
| 283.15 | 100.00 | 1231.06 |
| 283.15 | 10000.00 | 1285.85 |
| 283.15 | 20000.00 | 1335.74 |
| 283.15 | 30000.00 | 1381.4 |
| 283.15 | 40000.00 | 1424.94 |
| 283.15 | 50000.00 | 1464.43 |
| 283.15 | 60000.00 | 1502.23 |
| 283.15 | 70000.00 | 1537.63 |
| 283.15 | 80000.00 | 1571.96 |
| 283.15 | 90000.00 | 1604.68 |
| 283.15 | 100000.00 | 1635.63 |
| 288.15 | 100.00 | 1208.58 |
| 288.15 | 10000.00 | 1265.05 |
| 288.15 | 20000.00 | 1316.19 |
| 288.15 | 30000.00 | 1362.56 |
| 288.15 | 40000.00 | 1407.06 |
| 288.15 | 50000.00 | 1447.7 |
| 288.15 | 60000.00 | 1485.52 |
| 288.15 | 70000.00 | 1521.53 |
| 288.15 | 80000.00 | 1556.22 |
| 288.15 | 90000.00 | 1589.2 |
| 288.15 | 100000.00 | 1620.74 |
| 293.15 | 100.00 | 1186.09 |
| 293.15 | 10000.00 | 1244.14 |
| 293.15 | 20000.00 | 1296.86 |
| 293.15 | 30000.00 | 1344.06 |
| 293.15 | 40000.00 | 1389.16 |
| 293.15 | 50000.00 | 1430.7 |
| 293.15 | 60000.00 | 1469.0 |
| 293.15 | 70000.00 | 1505.7 |
| 293.15 | 80000.00 | 1540.77 |
| 293.15 | 90000.00 | 1574.27 |
| 293.15 | 100000.00 | 1605.01 |
| 298.15 | 100.00 | 1165.34 |
| 298.15 | 10000.00 | 1223.74 |
| 298.15 | 20000.00 | 1277.93 |
| 298.15 | 30000.00 | 1325.68 |
| 298.15 | 40000.00 | 1371.61 |
| 298.15 | 50000.00 | 1413.84 |
| 298.15 | 60000.00 | 1452.64 |
| 298.15 | 70000.00 | 1490.14 |
| 298.15 | 80000.00 | 1525.25 |
| 298.15 | 90000.00 | 1559.14 |
| 298.15 | 100000.00 | 1591.53 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 4731.33] | kPa | [240.93; 508.10] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.48340e+01 | |||
| Coefficient B | -3.02945e+03 | |||
| Coefficient C | -3.26710e+01 | |||
| Temperature range, min. | 240.93 | |||
| Temperature range, max. | 508.10 | |||
| Pvap | 1.33 | kPa | 240.93 | Calculated Property |
| Pvap | 8.18 | kPa | 270.62 | Calculated Property |
| Pvap | 33.60 | kPa | 300.30 | Calculated Property |
| Pvap | 104.03 | kPa | 329.99 | Calculated Property |
| Pvap | 262.34 | kPa | 359.67 | Calculated Property |
| Pvap | 567.19 | kPa | 389.36 | Calculated Property |
| Pvap | 1089.25 | kPa | 419.04 | Calculated Property |
| Pvap | 1905.84 | kPa | 448.73 | Calculated Property |
| Pvap | 3095.17 | kPa | 478.41 | Calculated Property |
| Pvap | 4731.33 | kPa | 508.10 | Calculated Property |
| Pvap | [2.57e-03; 4695.88] | kPa | [178.45; 508.20] |
KDB Vapor Pressure Data
|
| Equation | ln(Y) = A + B/T + C·ln(T) + D·T² + E/T² Y is Pvap in kPa, T in K | |||
| Coefficient A | 6.69693e+01 | |||
| Coefficient B | -5.78459e+03 | |||
| Coefficient C | -7.85881e+00 | |||
| Coefficient D | 7.10496e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 178.45 | |||
| Temperature range, max. | 508.20 | |||
| Pvap | 2.57e-03 | kPa | 178.45 | Calculated Property |
| Pvap | 0.16 | kPa | 215.09 | Calculated Property |
| Pvap | 2.70 | kPa | 251.73 | Calculated Property |
| Pvap | 19.81 | kPa | 288.37 | Calculated Property |
| Pvap | 87.11 | kPa | 325.01 | Calculated Property |
| Pvap | 273.04 | kPa | 361.64 | Calculated Property |
| Pvap | 678.92 | kPa | 398.28 | Calculated Property |
| Pvap | 1435.57 | kPa | 434.92 | Calculated Property |
| Pvap | 2705.52 | kPa | 471.56 | Calculated Property |
| Pvap | 4695.88 | kPa | 508.20 | Calculated Property |
| Pvap | [4.33; 4599.85] | kPa | [259.16; 507.60] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47929e+01 | |||
| Coefficient B | -3.02157e+03 | |||
| Coefficient C | -3.24450e+01 | |||
| Reference | Ambrose, Sprake, et al., 1974 | |||
| Temperature range, min. | 259.16 | |||
| Temperature range, max. | 507.60 | |||
| Pvap | 4.33 | kPa | 259.16 | Calculated Property |
| Pvap | 18.39 | kPa | 286.76 | Calculated Property |
| Pvap | 58.86 | kPa | 314.37 | Calculated Property |
| Pvap | 153.09 | kPa | 341.97 | Calculated Property |
| Pvap | 340.48 | kPa | 369.58 | Calculated Property |
| Pvap | 670.93 | kPa | 397.18 | Calculated Property |
| Pvap | 1201.74 | kPa | 424.79 | Calculated Property |
| Pvap | 1993.73 | kPa | 452.39 | Calculated Property |
| Pvap | 3107.44 | kPa | 480.00 | Calculated Property |
| Pvap | 4599.85 | kPa | 507.60 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetone.
Mixtures
- Acetonitrile + Acetone
- Benzene + Acetonitrile + Acetone + Methyl Alcohol
- Acetonitrile + Ethanol + Acetone
- Benzene + Acetonitrile + Ethanol + Acetone
- Acetonitrile + Acetone + Water
- 1,2-Ethanediol + Acetone
- 1,2-Ethanediol + Acetone + Methyl Alcohol
- 1,2-Ethanediol + Acetone + Water
- 1-Butanol + Acetone
- 1-Butanol + Acetone + Water
- 1-Hexene + Acetone
- 2-Propanol + Acetone
- 2-Propanol + Acetone + Methyl Alcohol
- 2-Propanol + Acetone + Methyl Alcohol + Water
- 2-Propanol + Acetone + Water
- Acetone + Acetic acid
- Acetone + Acetic acid + Water
- Acetic acid, butyl ester + Acetone
- Acetic acid, butyl ester + Acetone + Water
- Benzene + Acetone
Find more mixtures with Acetone.
Sources
- KDB Vapor Pressure Data
- Cheméo Relay (1.0)
- Crippen Method
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Study of Acoustic Parameters in Binary Mixture at Variable Frequencies
- Measurement and prediction of vapor-liquid equilibria of ternary systems containing ionic liquids
- Measurement and correlation of vapor liquid equilibria of binary systems containing the ionic liquids [EMIM][(CF3SO2)2N], [BMIM][(CF3SO2)2N], [MMIM][(CH3)2PO4] and oxygenated organic compounds respectively water
- Isobaric vapor liquid equilibria for mixtures of acetone, ethanol, and 2,2,4-trimethylpentane at 101.3 kPa
- A relative headspace method for Henry s constants of volatile organic compounds
- Vapor liquid equilibria for systems of diethyl carbonate and ketones and determination of group interaction parameters for the UNIFAC and ASOG methods
- Vapor liquid liquid equilibria of perfluorohexane +CO2 + methanol, +toluene, and +acetone at 313K
- Isobaric vapor liquid equilibria for acetone + methanol + lithium nitrate at 100 kPa
- Experimental isobaric vapour liquid liquid equilibrium data for the quaternary systems water (1) ethanol (2) acetone (3) n-butyl acetate (4) and water (1) ethanol (2) acetone (3) methyl ethyl ketone (4) and their partially miscible-constituent ternaries
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- 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)
- Solubility of sodium diclofenac in different solvents
- Solubilities of rutin in eight solvents at T = 283.15, 298.15, 313.15, 323.15, and 333.15K
- Measurements of the solubilties of m-phthalic acid in acetone, ethanol and acetic ether
- Solid liquid phase equilibrium and phase diagram for ternary o-nitrobenzoic acid p-nitrobenzoic acid acetone system at 283.15K and 313.15K
- Vapor liquid equilibria and interfacial tensions for the ternary system acetone + 2,2 -oxybis[propane] + cyclohexane and its constituent binary systems
- Phase equilibria and interfacial tensions in the systems methyl tert-butyl ether + acetone + cyclohexane, methyl tert-butyl ether + acetone and methyl tert-butyl ether + cyclohexane
- Measurement of solubility of erythromycin acetone solvate in aqueous acetone solution between 298K and 323K
- Solid liquid equilibria of the ternary system m-nitrobenzoic acid + p-nitrobenzoic acid + acetone
- 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
- Measurement and prediction of multicomponent diffusion coefficients in four ternary liquid systems
- Compact apparatus for rapid measurement of high-pressure phase equilibria of carbon dioxide expanded liquids
- Solubility of benzoic acid in acetone, 2-propanol, acetic acid and cyclohexane: Experimental measurement and thermodynamic modeling
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Solubility of alpha-form and beta-form of L-glutamic acid in different aqueous solvent mixtures
- Liquid densities of acetone and n-heptane and excess volumes of the binary system in a wide temperature and pressure range
- Determination of the solubility, dissolution enthalpy and entropy of Deflazacort in different solvents
- Measurement and correlation of solubility of benzamide in supercritical carbon dioxide with and without cosolvent
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
- Determination of the solubility, dissolution enthalpy and entropy of pyrene in different solvents
- Thermodynamics of the solubility of lomefloxacin in methanol, ethanol, 1-propanol, 2-propanol, acetone, and chloroform from 293.15 to 323.15 K
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid ethyl(2-hydroxyethyl)dimethyl-ammonium diethylphosphate using gas liquid chromatography
- Solid-liquid phase equilibrium of glyphosate in selected solvents
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Solubility of lansoprazole in different solvents
- Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
- Thermodynamic analysis and correlation of solubility of candesartan cilexetil in aqueous solvent mixtures
- Solid liquid equilibrium of 1-hydroxyethane-1,1-diphosphonic acid in different solvents
- Influence of sulfate-based anion ionic liquids on the separation factor of the binary azeotropic system acetone + methanol
- Isobaric vapor-liquid equilibria of the binary system acetone + acetone oxime methyl ether at 101.3 kPa
- Thermodynamics of ketone + amine mixtures. Part IX. Excess molar enthalpies at 298.15K for dipropylamine, or dibutylamine + 2-alkanone systems and modeling of linear or aromatic amine + 2-alkanone mixtures in terms of DISQUAC and ERAS
- Solubility of propanoic acid 3-(hydroxyphenylphosphinyl)-sodium salts in different solvent
- Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
- Correlation of solubility of pioglitazone hydrochloride in different binary solvents
- Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
- Thermodynamics of ketone + amine mixtures. Part X. Excess molarenthalpies at 298.15 K for N,N,N-triethylamine + 2-alkanone systems.Characterization of tertiary amine + 2-alkanone, and ofamino-ketone + n-alkane mixtures in terms of DISQUAC
- A novel dynamic recirculating apparatus for vapour-liquid equilibrium measurements at moderate pressures and temperatures
- Measurement and calculation of solid-liquid phase equilibrium for ternary 4-chlorophthalic anhydride + 3-chlorophthalic anhydride + acetone system
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- A Raman spectroscopic method for the determination of high pressure vapour liquid equilibria
- Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
- Measurements of activity coefficients at infinite dilution in vegetable oils and capric acid using the dilutor technique
- The solubility of mercaptosuccinic acid in water + (methanol, ethanol, acetone) mixtures from (278.15 to 333.15 K)
- Determination and correlation of cefoperazone solubility in different pure solvents and binary mixture
- Vapor-liquid equilibrium in the production of the ionic liquid, 1-hexyl-3-methylimidazolium bromide ([HMIm][Br]), in acetone
- Solid-liquid equilibrium of dicyandiamide in different solvents
- Measurement and correlation of the solubility of maleic anhydride in different organic solvents
- Thermodynamics of fenofibrate and solubility in pure organic solvents
- Measurement and correlation of the solubilities of tetra(5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy) neopentane in different pure solvents
- The determination and correlation of the solubility of naproxen in acetone and water mixtures
- Determination and correlation of solubility and solution thermodynamics of valnemulin hydrogen tartrate in different pure solvents
- High-pressure solubility of naproxen, nicotinamide and their mixture in acetone with supercritical CO2 as an anti-solvent
- Thermostabilities and solubilities of flame retardant bisphenol S-bis (5,5-dimethyl-1,3-dioxaphosphorinanyl-2-oxy phosphate ester) as a function of temperature
- Solubility and polymorphic forms of antibiotic lasalocid sodium in different organic solvents
- Thermodynamics of risperidone and solubility in pure organic solvents
- Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
- Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
- Solid-liquid equilibrium of sulbactam in pure solvents and binary solvent mixtures
- Separation of acetone and methanol azeotropic system using ionic liquid as entrainer
- Solubility and thermodynamic functions of cefazolin acid in pure and mixed solvents at (278.15 308.15) K
- Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
- Correlation of solubility and calculation of thermodynamic properties of guanidine nitrate in different solvents
- Thermodynamic analysis and correlation of solubility of Cefaclor in different solvents from 278.15 to 313.15 K
- Solubility of methylphosphonic acid in selected organic solvents
- Separation of pyridine from heptane with tricyanomethanide-based ionic liquids
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
- Thermodynamic models for determination of the solid-liquid equilibrium of oxytocin in (acetonitrile + acetone) binary solvent mixtures
- Activity coefficients at infinite dilution for different alcohols and ketones in [EMpy][ESO4]: Experimental data and modeling with PC-SAFT
- Measurement and correlation of ternary solid-liquid equilibrium of 2-methyl-1,4-naphthoquinone + phthalic anhydride + acetone system
- 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
- Solubility of D-phenylglycine methyl ester hydrochloride in water and in organic individual or mixed solvents: Experimental data and results of thermodynamic modeling
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Isothermal vapour-liquid equilibrium data for the binary systems 2-propanone + (2-butanol or propanoic acid)
- Coupled phase-reaction equilibrium for dihydromyrcene hydration system
- Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
- In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
- Isobaric vapor-liquid equilibrium for ternary mixtures of acetone + methanol + ionic liquids at 101.3kPa
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
- Isobaric vapor-liquid equilibrium for acetone + methanol system containing different ionic liquids at 101.3 kPa
- Gas solubilities of carbon dioxide in methanol, acetone, mixtures of methanol and water, and mixtures of methanol and acetone
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
- Measurements of activity coefficient at infinite dilution for organic solutes in tetramethylammonium chloride + ethylene glycol deep eutectic solvent using gas-liquid chromatography
- Solubility evaluation and thermodynamic modeling of beta-lapachone in water and ten organic solvents at different temperatures
- Solubility of 1-methyl-4-nitropyrazole in seventeen pure solvents at temperatures from 283.15 K to 323.15 K
- Tetramethylammonium chloride + glycerol deep eutectic solvent as separation agent for organic liquid mixtures: Assessment from experimental limiting activity coefficients
- High-pressure phase equilibrium data for carbon dioxide p dichloromethane p acetone and carbon dioxide p dichloromethane p acetone p N-acetylcysteine (NAC)
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- Solubility determination and correlation of cyromazine in sixteen pure solvents and mixing properties of solutions
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- The behavior of mercury in water, alcohols, monoethylene glycol and triethylene glycol II. Elemental mercury solubility in alcohols, ethers and acetone; gas plant mercury distribution; and speciation in monoethylene glycol solution
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Densities, viscosities, and refractive indices of binary and ternary mixtures of methanol, acetone, and chloroform at temperatures from (298.15-318.15) K and ambient pressure
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Solubility measurements and thermodynamic modeling of pyrazinamide in five different solvent-antisolvent mixtures
- Solubility and density of the disodium salt hemiheptahydrate of ceftriaxone in (acetone + water) at T=(298.15,308.15, and 318.15) K
- A novel non-intrusive microcell for sound-speed measurements in liquids. Speed of sound and thermodynamic properties of 2-propanone at pressures up to 160 MPa
- A thermodynamic study of the ketoreductase-catalyzed reduction of 2-alkanones in non-aqueous solvents
- Thermodynamics of binary mixtures of N-methyl-2-pyrrolidinone and ketone. Experimental results and modelling of the solid-liquid equilibrium and vapou-liquid equilibrium. The Modified UNIFAC (Do) model characterization
- Solubility of paroxetine hydrochloride hemi-hydrate in (water + acetone)
- Systems with ionic liquids: Measurement of VLE and c1 data and prediction of their thermodynamic behavior using original UNIFAC, mod. UNIFAC(Do) and COSMO-RS(Ol)
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- Physical properties of the binary systems methylcyclopentane with ketones (acetone, butanone and 2-pentanone) at T = (293.15, 298.15, and 303.15) K. New UNIFAC-VISCO interaction parameters
- (Vapour + liquid) equilibria for (2-ethoxypropene + acetone) and (2-ethoxypropene + butanone)
- Excess molar enthalpies and volumes of binary mixtures of nonafluorobutylmethylether with ketones at T = 298.15 K
- Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
- Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
- Measurement and correlation of solubility of trans-resveratrol in 11 solvents at T = (278.2, 288.2, 298.2, 308.2, and 318.2) K
- Enthalpies of solution of N,N,N0,N0-tetramethylurea in amides, dimethylsulphoxide, and acetone at 298.15 K
- Thermodynamic properties of acetone calculated from accurate experimental speed of sound measurements at low temperatures and high pressures
- Activity coefficients at infinite dilution measurements for organic solutes and water in the ionic liquid 4-methyl-N-butyl-pyridinium bis(trifluoromethylsulfonyl)-imide
- Activity coefficients at infinite dilution for solutes in the trioctylmethylammonium bis(trifluoromethylsulfonyl)imide ionic liquid using gas liquid chromatography
- Excess parameter studies on the binary mixtures of toluene with ketones at different temperatures
- 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.
- (Ternary liquid + liquid) equilibria for (water + acetone + alpha-pinene, or beta-pinene, or limonene) mixtures
- Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
- Measurements of activity coefficients at infinite dilution of organic compounds and water in isoquinolinium-based ionic liquid [C8iQuin][NTf2] using GLC
- 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
- Apparent molar volumes and compressibilities of tetrabutyl-ammonium bromide in organic solvents
- 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
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
- Solubility of diosgenin in different solvents
- 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
- Solubility of nicotinic acid in water, ethanol, acetone, diethyl ether, acetonitrile, and dimethyl sulfoxide
- 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
- Phase diagrams of acetonitrile or (acetone + water + EPPS) buffer phase separation systems at 298.15 K and quantum chemical modeling
- Measurement and prediction of the solubilities of aromatic polyimide monomers in supercritical carbon dioxide with acetone
- 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 coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- Measurement and correlation of solubility of Tetracycline hydrochloride in six organic solvents
- 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
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Solubilities of evodiamine in twelve organic solvents from T = (283.2 to 323.2) K
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds Part II: C18 fatty acids
- 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
- Thermodynamic properties of binary mixtures of the ionic liquid [emim][BF4] with acetone and dimethylsulphoxide
- On the solubility of nicotinic acid and isonicotinic acid in water and organic solvents
- 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 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 the ionic liquid trihexyltetradecylphosphonium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography at T = (313.15, 333.15, 353.15 and 373.15) K
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- 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
- Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
- Separation of sulfur compounds from alkanes with 1-alkylcyanopyridinium-based ionic liquids
- 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
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Effect of the alkyl side chain of the 1-alkylpiperidinium-based ionic liquids on desulfurization of fuels
- Measurement, correlation and dissolution thermodynamics of biological active chalcone in organic solvents at different temperatures
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-butyl-3-methylimidazolium methyl sulfate
- Experimental measurement and modelling of solubility of inosine-5'-monophosphate disodium in pure and mixed solvents
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- Extraction desulfurization process of fuels with ionic liquids
- An odd-even effect on solubility of dicarboxylic acids in organic solvents
- (Solid + liquid) phase equilibria of tetraphenyl piperazine-1,4-diyldiphosphonate in pure solvents
- VLE measurements using a static cell vapor phase manual sampling method accompanied with an empirical data consistency test
- Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
- Isothermal (vapor + liquid) equilibria for the binary mixtures of (propylene oxide + ethanol) and (propylene oxide + 1-propanol) at several temperatures
- (Liquid + liquid) equilibria for (water + 1-propanol or acetone + .beta.-citronellol) at different temperatures
- 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
- Solubility of daidzin in different organic solvents and (ethyl alcohol + water) mixed solvents
- Activity coefficients at infinite dilution for organic solutes and water in 1-ethyl-1-methylpyrrolidinium lactate
- Measurement and correlation of the solubility of genistin in eleven organic solvents from T = (283.2 to 323.2) K
- 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
- Solubility of tridecanedioic acid in pure solvent systems: An experimental and computational study
- Solubility measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
- Solution thermodynamics of valnemulin hydrogen fumarate in different pure solvents
- 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
- Ionic liquid 1-hexyl-3-methylimidazolium hexafluorophosphate, an efficient solvent for extraction of acetone from aqueous solutions
- Determination and correlation of pyridoxine hydrochloride solubility in different binary mixtures at temperatures from (278.15 to 313.15) K
- Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
- Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
- Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
- Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
- Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
- Determination and correlation of solubility and thermodynamic properties of L-methionine in binary solvents of water + (methanol, ethanol, acetone)
- Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
- Solvation of hydrocarbons in aqueous-organic mixtures
- Solubility of 3-chloro-N-phenylphthalimide in ten organic solvents from T = (288.15 to 323.15) K: Determination and modelling
- A 1-alkylcyanopyridinium-based ionic liquid in the separation processes
- Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
- Thermodynamics of amide + ketone mixtures. 1. Volumetric, speed of sound and refractive index data for N,N-dimethylformamide + 2-alkanone systems at several temperatures
- Determination and thermodynamic modeling of solid-liquid phase equilibrium for 3,5-dichloroaniline in pure solvents and ternary 3,5-dichloroaniline + 1,3,5-trichlorobenzene + toluene system
- Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
- Determination and modeling of the solubility of (limonin in methanol or acetone + water) binary solvent mixtures at T = 283.2 K to 318.2 K
- Thermodynamic models for determination of 3-chloro-N-phenylphthalimide solubility in binary solvent mixtures of (acetone, ethyl acetate or 1,4-dioxane + methanol)
- Solubility determination and thermodynamic modeling of 5-nitro-8- hydroxyquinoline in ten organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
- 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
- Determination and correlation of solubility of 4'-bromomethyl-2-cyanobiphenyl in acetone + (ethanol, n-propanol, n-butanol) mixtures
- Phase equilibria of the ternary systems of (water + diethyl carbonate) with acetone, or 2-butanone at four temperatures
- Thermodynamic study of the solubility of 2,4'-dihydroxydiphenyl sulfone in nine organic solvents from T = (278.15 to 313.15) K and thermodynamic properties of dissolution
- Solubility determination and thermodynamic modeling of 2,4-dinitroaniline in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
- Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
- 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
- Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
- Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
- Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
- Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- Solubility measurement and correlation of 4-nitrophthalimide in (methanol, ethanol, or acetone) + N,N-dimethylformamide mixed solvents at temperatures from 273.15 K to 323.15 K
- Solubility of N-phenylanthranilic acid in nine organic solvents from T = (283.15 to 318.15) K: Determination and modelling
- Thermodynamic functions of 1-methyl-4-(methylsulfonyl)benzene solubility in nine organic solvents from T = (278.15 to 318.15) K
- Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
- Solubility determination and thermodynamic modelling of allisartan isoproxil in different binary solvent mixtures from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility measurement and modelling of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in four groups mixed solvents
- Separation of ethylbenzene/styrene systems using ionic liquids in ternary LLE
- Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
- Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
- Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
- Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
- Solubility of L-histidine in different aqueous binary solvent mixtures from 283.15 K to 318.15 K with experimental measurement and thermodynamic modelling
- Determination and modeling of binary and ternary solid-liquid phase equilibrium for the systems formed by 3,5-dinitrobenzoic acid, m-nitrobenzoic acid and acetone
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Understanding the enhanced solubility of 1,3-benzenedicarboxylic acid in polar binary solvents of (acetone + water) at various temperatures
- Thermodynamic properties of L-Theanine in different solvents
- Thermodynamic study of solubility for 2-amino-4-chloro-6-methoxypyrimidine in twelve organic solvents at temperatures from 273.15 K to 323.15 K
- Determination and correlation of Avermectin B1a solubility in different binary solvent mixtures at temperatures from (283.15 to 313.15) K
- Solid-liquid phase equilibrium and dissolution properties of ethyl vanillin in pure solvents
- Solubility and solution thermodynamics of 2-methyl-4-nitroaniline in eleven organic solvents at elevated temperatures
- Solubility measurement and thermodynamic functions of 3-nitrobenzaldehyde in different solvents at elevated temperatures
- Determination and correlation of solubility of 11alpha,17alpha-dihydroxy-4-pregnene-3,20-dione in different solvents
- Solubility determination and modelling of 4-nitro-1,2-phenylenediamine in eleven organic solvents from T = (283.15 to 318.15) K and thermodynamic properties of solutions
- Solubility determination and thermodynamic modelling for 2-amino-4-chlorobenzoic acid in eleven organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility determination and modelling for phthalimide in mixed solvents of (acetone, ethyl acetate or acetonitrile + methanol) from (278.15 to 313.15) K
- Solubility determination and thermodynamic functions of 2-chlorophenothiazine in nine organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility and thermodynamic functions of tebuconazole in nine organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamic models for determination of solid liquid equilibrium of the 6-benzyladenine in pure and binary organic solvents
- Solubility of 2-isopropylimidazole in nine pure organic solvents and liquid mixture of (methanol + ethyl acetate) from T = (278.15 to 313.15) K: Experimental measurement and thermodynamic modelling
- Thermodynamic equilibrium of hydroxyacetic acid in pure and binary solvent systems
- Solubility determination and thermodynamic modelling of 3,5-dimethylpyrazole in nine organic solvents from T = (283.15 to 313.15) K and mixing properties of solutions
- Ternary and binary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + water between 298 and 343 K
- Thermodynamic functions for solubility of 3-nitro-o-toluic acid in nine organic solvents from T = (283.15 to 318.15) K and apparent thermodynamic properties of solutions
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on limiting activity coefficients
- Thermodynamic models for determination of the solid-liquid equilibrium of istradefylline in ethyl acetate plus (isopropanol, tetrahydrofuran, acetone) binary solvent mixtures
- Thermodynamic study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
- Dielectric study of H-bonded interactions in amyl alcohols with ketones and DMSO at T = 298.15 K
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- 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
- Quaternary and ternary LLE measurements for solvent (2-methyltetrahydrofuran and cyclopentyl methyl ether) + furfural + acetic acid + water between 298 and 343 K
- 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
- Isobaric vapour-liquid equilibrium measurements and extractive distillation process for the azeotrope of (N,N-dimethylisopropylamine + acetone)
- 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
- Improving the method of solution calorimetry for evaluation of the enthalpies of phase transitions and condensed state enthalpies of formation
- 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
- Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
- The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
- Solubility and thermodynamic properties of dirithromycin form A and form B in pure solvents and binary solvent mixture
- Research on the application of 7-chloro-quinaldine adducts in 7-chloro-quinaldine separation process
- Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
- Cosolvent effect on solubility of aripiprazole in mixed solvents and apparent thermodynamic analysis of dissolution process
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
- Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
- Thermochemistry of 1-bromoadamantane in binary mixtures of water aprotic solvent
- Physical properties and their corresponding changes of mixing for the ternary mixture acetone + n-hexane +water at 298.15K
- Volumetric studies and thermodynamics of viscous flow of hydroxamic acids in acetone +water solvent at temperatures 303.15 and 313.15K
- Enthalpies of solution of tetramethyl-bis-urea (Mebicarum) in amides and acetone at 298.15 K
- Effect of electrostatic interaction on thermochemical behavior of 12-crown-4 ether in various polar solvents
- Enthalpies of Solution of Glycilglycine in Water-Organic Solvent Media at 298.15 K
- Water as a solute in aprotic dipolar solvents. 1. D2O-H2O solute isotope effects on the enthalpy of water dissolution in acetone, tetrahydrofuran and 1,4-dioxane at 298.15 K
- Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
- Measurement and correlation of the solubility of maleic acid in acetone-ethyl acetate mixtures
- Determination of the solubility, dissolution enthalpy and entropy of 3-pentadecylphenyl acrylate in different organic solvents
- Solubility, dissolution enthalpy and entropy of L-Glutamine in mixed solvents of ethanol+water and acetone+water
- Measurement and correlation of phase diagram data for acetone andsulfate aqueous two-phase systems at different temperatures
- Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
- Calorimetric study of solvation of low polar solutes in propylene glycol and methyl cellosolve at 298 K
- Examination of hydrogen-bonding interactions between dissolved solutes and alkylbenzene solvents based on Abraham model correlations derived from measured enthalpies of solvation
- Use of quantitative structure property relationships to study the solvation process of 18-crown-6
- Influence of the composition of water organic mixtures and the properties of organic solvents on thermochemical characteristics of l-methionine dissolution at 298.15 K
- Effect of halogen substitution on the enthalpies of solvation and hydrogen bonding of organic solutes in chlorobenzene and 1,2-dichlorobenzene derived using multi-parameter correlations
- Thermodynamics of hydrogen bonding and van der Waals interactions of organic solutes in solutions of imidazolium based ionic liquids: "structure-property" relationships
- Thermodynamic of dissolution and hydrogen bond of the pyrrole, N-methylpyrrole with proton acceptors
- Enthalpies of solution and enthalpies of solvation of organic solutes in ethylene glycol at 298.15 K: Prediction and analysis of intermolecular interaction contributions
- Thermochemistry of hydrogen bonding of linear and cyclic amides inproton acceptors media
- Thermochemistry of hydrogen bonding of proton acceptors in the media of linear and cyclic amides. Cooperativity effects in multi-particle complexes of amides
- Isobaric specific heat capacities of emulsified kerosene at high temperature and pressure
- Experimental solubility and thermodynamic aspects of methylene blue in different solvents
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
- Dissociation Constants and Solubilities of Dalbergin and Nordalbergin in Different Solvents
- Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
- Solid Forms, Crystal Habits, and Solubility of Danthron
- Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
- Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
- Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
- Solubility of Agomelatine Crystal Form I and Form II in Pure Solvents and (Isopropanol + Water) Mixtures
- Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
- Measurement and Correlation of Solubility of Cefathiamidine in Water + (Acetone, Ethanol, or 2-Propanol) from (278.15 to 308.15) K
- Measurement and Correlation of the Solubility of Vanillic Acid in Eight Pure and Water + Ethanol Mixed Solvents at Temperatures from (293.15 to 323.15) K
- Solubility Measurement and Modeling of 4,4'-Dihydroxydiphenyl Sulfone in Nine Organic Solvents from T = (278.15 to 313.15) K and Thermodynamic Property of Dissolution
- Ternary and Binary LLE Measurements for Solvent (4- Methyl-2-pentanone and 2-Methyl-2-butanol) + Furfural + Water between 298 and 401 K
- Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
- Determination and Correlation of Solubilities for Succinic Acid in the Adipic Acid + Glutaric Acid + Acetone Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Acetone Mixture
- Quaternary, Ternary, and Binary LLE Measurements for 2-Methoxy-2-methylpropane + Furfural + Acetic Acid + Water at Temperatures between 298 and 307 K
- Quaternary, Ternary and Binary LLE Measurements for 2-Methoxy-2-methylbutane + Furfural + Acetic Acid + Water at Temperatures between 298 and 341 K
- Isobaric Vapor Liquid Equilibrium for Nine Binary Systems of Cracking C5 Fraction at 250 kPa
- Solubility Measurement and Thermodynamic Modeling of 4-Nitrophthalimide in Twelve Pure Solvents at Elevated Temperatures Ranging from (273.15 to 323.15) K
- Solubility of Fenofibrate in Different Binary Solvents: Experimental Data and Results of Thermodynamic Modeling
- Solubility of 3,7,9,11-Tetraoxo-2,4,6,8,10-pentaaza[3.3.3] Propellane (TOPAP) in Different Pure Solvents at Temperatures between 273.15 and 318.15 K
- Measurement and Correlation of the Solubility of p-Coumaric Acid in Nine Pure and Water + Ethanol Mixed Solvents at Temperatures from 293.15 to 333.15 K
- Solubility Determination and Modeling for 4,4'-Dihydroxydiphenyl Sulfone in Mixed Solvents of (Acetone, Ethyl Acetate, or Acetonitrile) + Methanol and Acetone + Ethanol from (278.15 to 313.15) K
- Measurement of Solubility of Thiamine Hydrochloride Hemihydrate in Three Binary Solvents and Mixing Properties of Solutions
- Solubility and Thermodynamic Behavior of Veramoss in Different Pure Solvents and {Ethanol + Water} Mixtures from T = 283.15 to 333.15 K
- Solubility Measurement and Correlation for e-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Five Organic Solvents at Temperatures between 283.15 and 333.15 K and Different Chloralkane + Ethyl Acetate Binary Solvents at Temperatures between 283.15 and 323.15 K
- Vapor Liquid Equilibrium Data for Binary Mixtures of Acetic Acid + Anisole, Acetone + Anisole, and Isopropanol + Anisole at Pressure 96.15 kPa
- Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
- Solubility Measurement and Correlation of Two Erlotinib Hydrochloride Polymorphs in Alcohols and Ketones from 273.15 to 323.15 K
- Solubility Measurement and the Correlation of 1-Naphthaleneacetic Acid in Pure and Methanol + Water Binary Solvents from T = (278.25 to 323.55) K
- Determination and Correlation of Solubility of Phenylbutazone in Monosolvents and Binary Solvent Mixtures
- Solubilities of 4',5,7-Triacetoxyflavanone in Fourteen Organic Solvents at Different Temperatures
- Determination and Correlation of Ethyl Vanillin Solubility in Different Binary Solvents at Temperatures from 273.15 to 313.15 K
- Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
- Pressurized-Synthetic Methodology for Solubility Determination at Elevated Temperatures with Application to Paracetamol in Pure Solvents
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) K
- Solubility of Benzoin in Six Monosolvents and in Some Binary Solvent Mixtures at Various Temperatures
- Determination of Infinite Dilution Activity Coefficients of Several Organic Solutes in N-Butylpyridinium Nitrate/N-Octylpyridinium Nitrate by Blend Inverse Gas Chromatography
- Experimental and Modeling Studies on the Solubility of 2-Chloro-N-(4-methylphenyl)propanamide (S1) in Binary Ethyl Acetate + Hexane, Toluene + Hexane, Acetone + Hexane, and Butanone + Hexane Solvent Mixtures Using Polythermal Method
- Measurement and Correlation of Solubility of Two Isomers of Cyanopyridine in Eight Pure Solvents from 268.15 K to 318.15 K
- Thermodynamic Functions for Solubility of 1-Hydroxybenzotriazole in Sixteen Solvents at Temperatures from (278.15 to 313.15) K and Mixing Property of Mixtures
- Determination and Correlation of Solubility of Quetiapine Fumarate in Nine Pure Solvents and Two Aqueous Binary Solvents
- Solubility in Different Solvents, Crystal Polymorph and Morphology, and Optimization of Crystallization Process of AIBN
- Solubility Modeling and Mixing Thermodynamics of Thiamphenicol in Water and Twelve Neat Organic Solvents from T = (278.15 to 318.15) K
- Synthesis and Solubility of 5,5-Dimethyl-2-(phenyl(phenylamino)methyl)-1,3,2-dioxaphosphinane 2-oxide in Selected Solvents between 278.15 K and 347.15 K
- Isothermal Vapor-Liquid Equilibria for Binary Mixtures of Methyl Nonafluorobutyl Ether + Acetone, Cyclopentyl Methyl Ether, Ethyl Acetate, n-Heptane, Methanol, and Toluene
- Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
- Solubility Measurement and Correlation of Fosfomycin Sodium in Six Organic Solvents and Different Binary Solvents at Temperatures between 283.15 and 323.15 K
- Determination and Correlation of Solubility and Thermodynamic Properties of trans-Cinnamyl Alcohol in Pure and Binary Solvents from 253.15 K to 293.15 K
- Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
- Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
- Determination, Correlation, and Application of Sodium l-Ascorbate Solubility in Nine Pure Solvents and Two Binary Solvents at Temperatures from 278.15 to 323.15 K
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Solution Thermodynamics of Benzotriazole in Different Pure Solvents
- Solubility of Ionic Liquid [Bmim]Ac in Supercritical CO2 Containing Different Cosolvents
- Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
- Aniracetam Solubility in Pure and Binary Solvents: Effect of Molecular Interaction and Analysis of Crystallized Products
- Solubility Measurement and Thermodynamic Modeling of Benzoic Acid in Monosolvents and Binary Mixtures
- 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
- Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
- Solubility Measurement and Modeling of 1-(3-nitrophenyl)Ethanone and 1-(4-nitrophenyl)Ethenone in Nine Pure Organic Solvents from T = (278.15 to 318.15) K and Mixing Properties of Solutions
- Determination of Solubility and Thermodynamic Properties of Benzophenone in Different Pure Solvents
- Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
- Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
- Solubility Determination and Correlation for Pyridoxal 5-Phosphate Monohydrate in Different Binary Solvents from 278.15 K to 318.15 K
- Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
- Determination and Correlation of the Solubility of l-Fucose in Four Binary Solvent Systems at the Temperature Range from 288.15 to 308.15 K
- Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
- Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Isobaric Vapor-Liquid Equilibrium Data for the Acetone + Hexamethyl Disiloxane + Ethyl Acetate Ternary System at 101.3 kPa: Determination and Correlation
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
- Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
- Measurement and Correlation of Solubility of 3-Hydroxy-2-naphthoic Acid in Ten Pure and Binary Mixed Organic Solvents from T = (293.15 to 333.15 K)
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Solubility of Diflufenican in Pure and Binary Solvent Systems
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Solubility Determination and Correlation of Glibenclamide in 11 Monosolvents and (Acetone + Acetonitrile) Binary Solvents from 283.15 K to 323.15 K
- Solubility Measurement and Thermodynamic Properties of Levetiracetam in Pure and Mixed Solvents
- Determination and Modeling of Solid-Liquid Equilibrium for Ternary Systems of Terephthaldialdehyde + 4-Hydroxybenzaldehyde + Ethyl Acetate/Acetone
- Solid-Liquid Equilibrium of Isomaltulose in Five Pure Solvents and Four Binary Solvents from (283.15 to 323.15) K
- Solubility Measurement and Correlation of Probenecid in 12 Pure Organic Solvents and Thermodynamic Properties of Mixing of Solutions
- Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
- Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Solubility Determination and Correlation of Warfarin Sodium 2-Propanol Solvate in Pure, Binary, and Ternary Solvent Mixtures
- Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
- Measurement and Correlation of the Solubility of Mifepristone in Eight Pure and Water + Methanol Mixed Solvents at Temperatures from 273.15 to 318.15 K
- Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
- Solubility Determination and Thermodynamic Modeling of Buprofezin in Different Solvents and Mixing Properties of Solutions
- Solubility in Different Solvents, Correlation, and Solvent Effect in the Solvent Crystallization Process of Iohexol
- Liquid Liquid Equilibrium Data for the Separation of Acetone from n-Heptane Using Four Imidazolium-Based Ionic Liquids
- Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
- Experimental Data and Thermodynamics Modeling (PC-SAFT EoS) of the {CO2 + Acetone + Pluronic F-127} System at High Pressures
- Binary Solid-Liquid Solubility Determination and Model Correlation of Quizalofop-p-ethyl in Different Pure Solvents
- Solid-Liquid Equilibrium of Azacyclotridecan-2-one in 15 Pure Solvents from T = 273.15 to 323.15 K: Experimental Determination and Thermodynamic Modeling
- Vapor Liquid Equilibrium Data for 2,3-Pentanedione + (Acetaldehyde or Acetone) at (100, 150, and 200) kPa
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Solubility, Model Correlation, and Solvent Effect of 2-Amino-3-methylbenzoic Acid in 12 Pure Solvents
- Solubility and Solution Thermodynamics of 3-Nitrophthalonitrile in 12 Neat Solvents at Temperatures from 278.15 to 323.15 K
- Solubility Measurement, Correlation, and Molecular Interactions of 3-Methyl-6-nitroindazole in Different Neat Solvents and Mixed Solvents from T = 278.15 to 328.15 K
- Equilibrium Solubility, Model Correlation, and Solvent Effect of Indole-3-acetic Acid in Twelve Pure Solvents
- Measurement and Correlation of Solubility of Calcium Formate (Form alpha) in Different Binary Solvent Mixtures at Temperatures from 283.15 to 323.15 K
- Determination and Correlation of Solubility of Borneol, Camphor, and Isoborneol in Different Solvents
- Solubility Study of (2E)-1-(3-Pyridyl)-3-(dimethylamino)-2-propen-1-one in Different Pure Solvents and Binary Solvent Mixtures from 278.15 to 328.15 K
- Experimental Measurements of the {CO2 (1) + Acetone (2) + Ivermectin (3)} System at High Pressure
- Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
- Solubility Measurement and Thermodynamic Model Correlation of 5-Nitrosalicylaldehyde in Different Solvents
- o-Nitrophenylacetonitrile Solubility in Several Pure Solvents: Measurement, Correlation, and Solvent Effect Analysis
- Measurement and Correlation of Solubilities of 5,5'-Dinitramino-3,3'-bi[1,2,4-triazolate] Carbohydrazide Salt (CBNT) in Various Pure Solvents and a Binary Mixture (Dimethyl Sulfoxide + Water) from 298.15 to 343.15 K
- Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
- Solubility and Solvent Effect of Acetamiprid in Thirteen Pure Solvents and Aqueous Solutions of Ethanol
- Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
- Solubility of d-Aspartic Acid in Several Neat Solvents: Determination, Modeling, and Solvent Effect Analysis
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- Solid-Liquid Equilibrium Solubility, Thermodynamic Properties, and Molecular Simulation of Phenylphosphonic Acid in 15 Pure Solvents at Different Temperatures
- Determination and Correlation of Solubilities of 1,3,5-Trifluoro-2,4,6-triiodobenzene in Different Solvents from 289.25 to 332.15 K
- Solubility Determination, Correlation, and Solute-Solvent Molecular Interactions of 5-Aminotetrazole in Various Pure Solvents
- Solubility Determination and Thermodynamic Mixing Properties of 5-Methyl-2-pyrazinecarboxylic Acid in Different Solvents
- Solubility and Thermodynamic Modeling of Sulfanilamide in 12 Mono Solvents and 4 Binary Solvent Mixtures from 278.15 to 318.15 K
- Solubility Measurement and Thermodynamic Modeling for o-Toluenesulfonamide in 16 Solvents from T = 273.15 to 323.85 K
- Binary Equilibrium Solubility of Amidinothiourea in Monosolvents: Experimental Determination, Model Correlation, and Solvent Effect Analysis
- The Research and Measurement about the Solubility of l-Serine in Eight Common Pure Solvents and Four Binary Mixed Solvents for T = (278.15-333.15) K
- Measurement and Correlation of Solubility of Marbofloxacin in 12 Pure Solvents from 283.15 to 328.15 K
- Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
- Saturated Solubility and Thermodynamic Evaluation of l-Tryptophan in Eight Pure Solvents and Three Groups of Binary Mixed Solvents by the Gravimetric Method at T = 278.15-333.15 K
- Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
- Solubility and Thermodynamic Modeling of Dimethyl Terephthalate in Pure Solvents and the Evaluation of the Mixing Properties of the Solutions
- Solubility Determination of 2-Chloronicotinic Acid and Analysis of Solvent Effect
- Measurement and Correlation of the Solubility of Dienogest in Twelve Pure and Water + Methanol Binary Solvents at Temperatures from 273.15 to 318.15 K
- Solubility and Data Correlation of b-Arbutin in Different Monosolvents from 283.15 to 323.15 K
- Solubility Behavior and Data Modeling of l-Proline in Different Neat and Binary Solvent Systems
- Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Surface Tension of Pure Liquids and Binary Liquid Mixtures
- Excess Molar Enthalpies for Binary Mixtures of Ethanol + Acetone, + Octane, + Cyclohexane and 1-Propanol + Acetone, + Octane, + Heptane at 323.15
- Experimental Densities and Excess Volumes for Binary Mixtures Containing Propionic Acid, Acetone and Water from 283.15 K to 323.15 K at Atmospheric Pressure
- Liquid-Liquid Equilibria of Water + Benzonitrile + Propanone, or + Dimethylsulfoxide
- Measurement of Activity Coefficients of Solutes at Infinite Dilution in (Dimethyl Sulfoxide + Acetamide, or Formamide, or Urea) Using Gas Liquid Chromatography at the Temperature 298.15 K
- Surface Tension and Interfacial Tension of Binary Organic Liquid Mixtures
- Conductivities and Viscosities of the Ionic Liquid [bmim][PF6] + Water + Ethanol and [bmim][PF6] + Water + Acetone Ternary Mixtures
- Phase Behavior, Densities, and Isothermal Compressibility of CO2 + Pentane and CO2 + Acetone Systems in Various Phase Regions
- Measurement of Henry s Law Constants for Acetone, 2-Butanone, 2,3-Butanedione, and Isobutyraldehyde Using a Horizontal Flow Reactor
- Phase Behavior, Densities and Isothermal Compressibility of CO2 + Pentane + Acetone Ternary System in Various Phase Regions
- Excess Molar Volumes and Surface Tensions of Xylene with Acetone or 2-Butanone at 298.15 K
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- Density, Viscosity, and Excess Properties of Binary Liquid Mixtures of Propylene Carbonate with Polar and Nonpolar Solvents
- Vapor Liquid Equilibrium for Binary System of 2-Propanol + 2-Ethoxy-2-methylpropane and Ethyl Ethanoate + 2-Ethoxy-2-methylpropane at 333 K and 2-Propanone + 2-Ethoxy-2-methylpropane at 323 K
- Densities and Excess Molar Volumes for Acetone + Propionic Acid + Water from (283.15 to 323.15) K at Atmospheric Pressure
- Pressure-Density-Temperature Behavior of CO2/Acetone, CO2/Toluene, and CO2/Monochlorobenzene Mixtures in the Near-Critical Region
- Solubility of 11r-Hydroxy-16r,17r-Epoxyprogesterone in Different Solvents between 283 K and 323 K
- Determination of Henry s Law Constants and Activity Coefficients at Infinite Dilution of Flavor Compounds in Water at 298 K with a Gas-Chromatographic Method
- Measurement of the Phase Behavior of the Ternary System Carbon Dioxide + Acetone + Phenanthrene
- Isobaric Vapor-Liquid Equilibrium of Acetone + Methanol System in the Presence of Calcium Bromide
- Measurement of Isobaric Vapor - Liquid Equilibria of Dimethyl Carbonate with Acetone, 2-Butanone and 2-Pentanone at 101.3 kPa and Density and Speed of Sound at 298.15 K
- Solubility of Propyl p-hydroxybenzoate in Supercritical Carbon Dioxide with and without Cosolvent
- Vapor Liquid Equilibrium for Binary System of 2-Propanol + 1,1-Diethoxyethane at 353 K and Ethyl ethanoate + 1,1-Diethoxyethane at 348 K and 2-Propanone + 1,1-Diethoxyethane at 328 K
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Vapor-Liquid Equilibria of the Carbon Dioxide + Acetone System at Pressures from (2.36 to 11.77) MPa and Temperatures from (333.15 to 393.15) K
- Solubility of DL-p-hydroxyphenylglycine Sulfate in Binary Acetone + Water Solvent Mixtures
- Solubility of Aspirin in Supercritical Carbon Dioxide with and without Acetone
- Densities, Refractive indices and Viscosities for Binary and Ternary Mixtures of Acetone, Ethanol and 2,2,4-Trimethylpentane at T = (288.15, 298.15, and 308.15) K
- Isothermal and Isobaric Vapor-Liquid Equilibria of the Ternary System of 2,2-Dimethoxypropane + Acetone + Methanol
- Solubility of Puerarin in Water, Ethanol, and Acetone from (288.2 to 328.2) K
- Solubility of Lovastatin in Acetone, Methanol, Ethanol, Ethyl Acetate, and Butyl Acetate between 283 K and 323 K
- Ternary Diffusion Coefficients of Glycerol + Acetone + Water by Taylor Dispersion Measurements at 298.15 K
- Solubility of Erythritol in Different Solvents
- Dynamic Viscosities of the Binary Systems Cyclohexane and Cyclopentane with Acetone, Butanone, or 2-Pentanone at Three Temperatures T ) (293.15, 298.15, and 303.15) K
- Solubility of 16.alpha.,17.alpha.-Epoxyprogesterone in Six Different Solvents
- Solubility of Ceftriaxone Disodium in Acetone, Methanol, Ethanol, N,N-Dimethylformamide, and Formamide between 278 and 318 K
- Solubility of p-Nitrobenzoic Acid in Supercritical Carbon Dioxide with and without Cosolvents
- 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
- Determination of Partitioning Coefficients of Numerous Organic Solutes between a Long-Chain Aliphatic Alcohol and the Gas Phase as a Function of Temperature
- Vapor Liquid Equilibrium for Six Binary Systems of C4-Hydrocarbons + 2-Propanone
- Solubility of Organic Systems Containing 1,4-Dioxan-2-one
- 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
- Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
- Liquid-Liquid Equilibrium of (Water + Acetone) with Cumene or r-Methylstyrene or Phenol at Temperatures of (323.15 and 333.15) K
- Solubility of Erythromycin A Dihydrate in Different Pure Solvents and Acetone + Water Binary Mixtures between 293 K and 323 K
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Solubility and Metastable Zone Width of 1-Keto-1,2,3,4-tetrahydro-6-methylcarbazole in Acetone
- Henry s Constants of 1-Alkanols and 2-Ketones in Salt Solutions
- Phase Boundaries of CO2 + Toluene, CO2 + Acetone, and CO2 + Ethanol at High Temperatures and High Pressures
- Measurement and Correlation of Solubilities of Luteolin in Organic Solvents at Different Temperatures
- Solubility and Melting Properties of Salicylic Acid
- Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
- Vapor-Liquid Equilibrium for Binary Systems of Diacetyl with Methanol and Acetone
- Solubility and Melting Properties of Salicylamide
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Diffusion Coefficients of Aromatic Compounds at Infinite Dilution in Binary Mixtures at 298.15 K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Ionic Liquids as Entrainers in Extractive Distillation: Isobaric Vapor-Liquid Equilibria for Acetone + Methanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate
- Solubility of 4-(3,4-Dichlorophenyl)-1-tetralone in Some Organic Solvents
- Solubility of Xylitol in Ethanol, Acetone, N,N-Dimethylformamide, 1-Butanol, 1-Pentanol, Toluene, 2-Propanol, and Water
- Solubilities of Triphenylphosphine in Ethanol, 2-Propanol, Acetone, Benzene, and Toluene
- Solubility of Acephate in Different Solvents from (292.90 to 327.60) K
- Solubility of a-Carotene in Binary Solvents Formed by Some Hydrocarbons with 2,5,8-Trioxanonane, 2-Propanone, and Cyclohexanone
- Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
- Solubility of Clopidogrel Hydrogen Sulfate (Form II) in Different Solvents
- Measurement and Correlation of Griseofulvin Solubility in Different Solvents at Temperatures from (281.95 to 357.60) K
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Butyl-3-methyl-pyridinium Trifluoromethanesulfonate
- Solubilities of Nizatidine in Water, Methanol, Ethanol, Acetone, and Ethyl Acetate from (273.15 to 343.15) K
- Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
- Solubility of Anthracene in C1-C3 Alcohols from (298.2 to 333.2) K and Their Mixtures with 2-Propanone at 298.2 K
- Solubility of Sulpiride in Pure Organic Solvents between (278 and 333) K
- Excess Molar Enthalpies of CO2 + Acetone at Pressures from (9.00 to 18.00) MPa and Temperatures from (313.15 to 333.15) K
- Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
- Solubility of Physalin D in Ethanol, Methanol, Propanone, Trichloromethane, Ethyl Ethanoate, and Water at Temperatures from (283.2 to 313.2) K
- Solubilities of Ibuprofen in Different Pure Solvents
- Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Solubility of CO2 in Propanone, 1-Ethyl-3-methylimidazolium Tetrafluoroborate, and Their Mixtures
- Solubility of Andrographolide in Various Solvents from (288.2 to 323.2) K
- Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
- Solubility of Form III Piracetam in a Range of Solvents
- Measurement and Correlation of Solubility of Cefuroxime Acid in Pure and Binary Solvents at Various Temperatures
- Determination of Activity Coefficients at Infinite Dilution of 35 Solutes in the Ionic Liquid, 1-Butyl-3-methylimidazolium Tosylate, Using Gas-Liquid Chromatography
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- High-Pressure Multiphase Behavior of the Ternary Systems (Ethene + Water + Acetone) and (Ethane + Water + Acetone)
- Solubility and Crystal Size of Sirolimus in Different Organic Solvents
- Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
- Solubility of Florfenicol in Different Solvents at Temperatures from (278 to 318) K
- Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
- Solid Liquid Phase Equilibrium and Phase Diagram for the Ternary Carbamazepine Succinic Acid Ethanol or Acetone System at (298.15 and 308.15) K
- Influence of Typical Impurities on the Surface Tension Measurements of Binary Mixtures of Water and the Ionic Liquids 1-Butyl-3-Methylimidazolium Tetrafluoroborate and Chloride
- Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurements of Activity Coefficients at Infinite Dilution for Organic Solutes and Water in the Ionic Liquid 1-Butyl-1-methylpiperydinium Thiocyanate
- Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
- Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
- Critical Assessment of CO2 Solubility in Volatile Solvents at 298.15 K
- Solubilities of 3-Carboxy-3-hydroxypentanedioic Acid in Ethanol, Butan-1-ol, Water, Acetone, and Methylbenzene
- Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
- Solubility of CO2 in Alcohols, Glycols, Ethers, and Ketones at High Pressures from (288.15 to 318.15) K
- Measurement and Correlation for the Solubility of Dimethyl 1,4-Cyclohexanedione-2,5-dicarboxylate in Different Solvents at Temperatures from (278.15 to 323.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Influence of Some Ionic Liquids Containing the Trifluoromethanesulfonate Anion on the Vapor Liquid Equilibria of the Acetone + Methanol System
- Thermodynamics of Ketone + Amine Mixtures. Part VIII. Molar Excess Enthalpies at 298.15 K for n-Alkanone + Aniline or + N-Methylaniline Systems
- Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Antisolvent Precipitation of Vitamin B6: A Thermodynamic Study
- 1-Ethyl-3-methylimidazolium Dicyanamide as a Very Efficient Entrainer for the Extractive Distillation of the Acetone + Methanol System
- Vapor Liquid Equilibrium Measurements of the Binary Mixtures Nitrogen + Acetone and Oxygen + Acetone
- Solubility of L-Phenylalanine Anhydrous and Monohydrate Forms: Experimental Measurements and Predictions
- Solubility of 6-Chloropyridazin-3-amine in Different Solvents
- Solubilities of 3-Methoxy-N-phenylaniline and 3-(Methylthio)-N-phenylaniline in Five Organic Solvents (285 K to 333.75 K)
- Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
- Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
- Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
- Solubility of CO2 in Acetone, 1-Butyl-3-methylimidazolium Tetrafluoroborate, and Their Mixtures
- Measurement and Correlation of the Solubility of Febuxostat in Four Organic Solvents at Various Temperatures
- Solubility of the Metastable Polymorph of Piracetam (Form II) in a Range of Solvents
- Solubility of 2-Hydroxybenzoic Acid in Water, 1-Propanol, 2-Propanol, and 2-Propanone at (298.2 to 338.2) K and Their Aqueous Binary Mixtures at 298.2 K
- Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
- Determination and Correlation of Solubility of Tris(3-hydroxypropyl)phosphine Oxide in Selected Solvents
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- Solid Liquid Equilibria of Ternary 4-Nitro-2-benzofuran-1,3-dione + 5-Nitro-2-benzofuran-1,3-dione + 2-Propanone at 283.15 K and 323.15 K
- Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
- Liquid Liquid Equilibrium for the Ternary System Acetone Oxime Methyl Ether Acetone Water
- Solubilities of Rutaecarpine in Twelve Organic Solvents from (283.2 to 323.2) K
- Solubility Measurement and Modeling for 2-Benzoyl-3-chlorobenzoic Acid and 1-Chloroanthraquinone in Organic Solvents
- Solubilities of 4-Bromo-1,8-naphthalic Anhydride in Different Pure Solvents and Binary Solvent Mixtures with the Temperature Range from (278.15 to 333.15) K
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
- Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Solubility of Hesperetin in Mixed Solvents
- Vapor Liquid Equilibrium for the 1,1,1-Trifluorotrichloroethane + Sulfuryl Chloride System at 101.3 kPa
- Fluid Phase Behavior of Nitrogen + Acetone and Oxygen + Acetone by Molecular Simulation, Experiment and the Peng Robinson Equation of State
- Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
- Measurement and Correlation of Solubility of Azithromycin Monohydrate in Five Pure Solvents
- Solubility of 1-Fluoro-4-(methylsulfonyl)benzene in Five Pure Organic Solvents at Temperatures from (288.40 to 331.50) K
- Enthalpies of .beta.-Alanine Dissolution in Some Water + Organic Mixtures at 298.15 K
- Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
- Solubility of 4-Hydroxybenzaldehyde in Supercritical Carbon Dioxide with and without Cosolvents
- Dissociation Constants and Solubilities of Daidzein and Genistein in Different Solvents
- Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
- Measurement and Correlation of Solubility and Dissolution Thermodynamic Properties of Furan-2-carboxylic Acid in Pure and Binary Solvents
- Measurement and Correlation for Solubility of L-valine in Water, Ethanol, N,N-Dimethylformamide, Acetone, and Isopropyl alcohol between 293.15 and 343.15 K
- Experimental Measurements and Modeling of the Solubility of Aceclofenac in Six Pure Solvents from (293.35 to 338.25) K
- Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of Cefixime Trihydrate in Seven Pure Solvents
- Measurement and Correlation of the Solubility of L-Carnitine in Different Pure Solvents and Ethanol Acetone Solvent Mixture
- Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
- Measurement and Correlation of Solubility of l-Valine in Water + (Ethanol, N,N-Dimethylformamide, Acetone, Isopropyl Alcohol) from 293.15 K to 343.15 K
- 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
- Solubility and Thermodynamic Functions of Isatin in Pure Solvents
- Solubility of Ibuprofen Sodium Dihydrate in Acetone + Water Mixtures: Experimental Measurement and Thermodynamic Modeling
- Measurement and Correlation of Solubility of Calcium-l-lactate Pentahydrate in Ethanol + Water and Acetone + Water Systems
- Phase equilibrium study of binary and ternary mixtures of ionic liquids + acetone + methanol
- Solubilities of 1,1'-[1,2-Ethanediylbis(oxy-1,2-ethanediyl)]bis-[3-methyl-1H-imidazolium-1-yl] Dihexafluorophosphate in Water, Methanol, Ethanol, Dimethylformamide, Dimethyl Sulfoxide, and (Acetone + Water) Binary Solvent Mixtures
- Liquid-liquid equilibria for the system acetone + solketal + glycerol at 303.2, 313.2 and 323.2 K
- Solubility of Two Polymorphs of Erlotinib Hydrochloride in Isopropanol and Acetone from (273.15 to 303.15) K
- Solubilities of Adipic Acid and Succinic Acid in Glutaric Acid + Acetone or n-butanol Mixture
- Isobaric Vapor Liquid Equilibrium for Acetone + Methanol + Phosphate Ionic Liquids
- Solubilities of 1,3,2-Dioxaphosphorinane-2-methanol-a,5,5-trimethyl-a-phenyl-2-oxide in Selected Solvents between 278.15 K and 343.15 K
- Thermodynamic Models for Determination of the Solubility of Sulfanilic Acid in Different Solvents at Temperatures from (278.15 to 328.15) K
- Solution Thermodynamics of Imidazolium-Based Ionic Liquids and Volatile Organic Compounds: Benzene and Acetone
- Solubility and Solution Thermodynamics of Diphenoxylate in Different Pure Solvents
- Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
- Solubility of 3,3'-(Oxidi-2,1-ethanediyl)bis[1-methyl-imidazolium] Dihexafluorophosphate in Water, Methanol, Ethanol, Acetone, and Acetonitrile and Binary Mixtures (Water + DMF) from (283.00 to 323.00) K
- Solubility of 2,5-Di-tert-butylhydroquinone and Process Design for Its Purification Using Crystallization
- Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Solubility Determination and Thermodynamic Models for 2-Methylnaphthalene in Different Solvents from T = (278.15 to 303.15) K
- Liquid Liquid Equilibrium for the Ternary System of Water + Acetone + Dihydromyrcenol at 358 K to 368 K under 0.8 MPa
- Experimental Investigation of the Solubility of CO2 in (Acetone + Water)
- Solubility of KCl and MgCl2 in Binary Solvents Formed by Acetone and Water in the Temperature Range between (293.15 and 323.15) K
- Surface Tension of the Ternary System Water + Acetone + Toluene
- Solubility of a-Sitosteryl Maleate and Stigmasteryl Maleate in Acetone and Ethyl Acetate
- Solubilities of 2,4,8,10-Tetraoxa-3,9-diphosphaspiro[5.5]undecane-3,9-dimethanol, r,r,rcents,rcents-tetramethyl-3,9-dioxide in Selected Solvents
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- Solubility of Flavonoids in Organic Solvents
- Measurement and Correlation of Solubility of Xylitol in Binary Ethanol + Acetone Solvent Mixtures with the Combined Nearly Ideal Binary Solvent/ Redlich-Kister Equation
- Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
- Solubility of Cyclotrimethylenetrinitramine (RDX) in Binary Solvent Mixtures
- Solubility of Irbesartan (Form A) in Different Solvents between 278 K and 323 K
- Solubility of Oleanolic Acid in Various Solvents from (288.3 to 328.3) K
- Ionic Conductivity of Selected 2:1 Electrolytes in Dilute Solutions of Mixed Aqueous Organic Solvents at 298.15 K
- Solubility of Imidacloprid in Different Solvents
- Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-1,4-dihydroxy Phenylene in the Selected Solvents
- Experimental Determination of Solubilities of Betulin in Acetone + Water and Ethanol + Water Mixed Solvents at T ) (278.2, 288.2, 298.2, 308.2, and 318.2) K
- Solubility of 2-(4-Ethylbenzoyl)benzoic Acid in Eleven Organic Solvents between 279.55 K and 343.15 K
- Solubility of Tetrahydroxybenzophenone (THBP) in Acetone
- Solubility of Dioxopromethazine Hydrochloride in Different Solvents
- Solubility of Trimethoprim (TMP) in Different Organic Solvents from (278 to 333) K
- Diffusion Coefficients of Organic Compounds at Infinite Dilution in Mixtures Involving Associating Compounds. Experimental Determination and Modeling by Group Contribution Methods
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Solubility of Acetylsalicylic Acid in Ethanol, Acetone, Propylene Glycol, and 2-Propanol
- Vapor Liquid Equilibrium for Binary Systems of 2,3-Pentanedione with Diacetyl and Acetone
- Isobaric Vapor Liquid Equilibria for Binary Systems of Acetone + Isopropenyl Acetate, 2-Butanone + Isopropenyl Acetate, and Isopropenyl Acetate + Acetylacetone at 101.3 kPa
- Solubility of p-Methylbenzene Sulfonic Acid in Pure and Modified Supercritical Carbon Dioxide
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- Density, Speed of Sound, and Derived Thermodynamic Properties of Ionic Liquids [EMIM]+[BETI]- or ([EMIM]+[CH3(OCH2CH2)2OSO3]- + Methanol or + Acetone) at T = (298.15 or 303.15 or 313.15) K
- Solubilities of Stearic Acid in Organic Solvents and in Azeotropic Solvent Mixtures
- Solubilities of Adefovir Dipivoxil in Different Binary Solvents at 298.15 K
- Solubility of Rifapentine in Different Organic Solvents
- Solubilities of Diphenylphosphinic Acid in Selected Solvents
- solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
- Solubility of Lovastatin in Acetone + Water Solvent Mixtures
- Solubility of Hesperetin in Various Solvents from (288.2 to 323.2) K
- Densities and Viscosities of 1-Butyl-3-methylimidazolium Tetrafluoroborate + Molecular Solvent Binary Mixtures
- Solubility of Lovastatin in Ethyl Acetate, Propyl Acetate, Isopropyl Acetate, Butyl Acetate, sec-Butyl Acetate, Isobutyl Acetate, tert-Butyl Acetate, and 2-Butanone, between (285 and 313) K
- Solubility of Isoniazid in Various Organic Solvents from (301 to 313) K
- Solubility of 11 -Hydroxypregna-1,4,16-triene-3,20-dione in Different Solvents
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Solubility of 1,6,6-Trimethyl-6,7,8,9-tetrahydrophenanthro[1,2-b]furan-10,11-dione in Four Organic Solvents from (283.2 to 323.3) K
- Measurement of Infinite Dilution Activity Coefficients of Alcohols, Ketones, and Aromatic Hydrocarbons in 4-Methyl-N-butylpyridinium Tetrafluoroborate and 1-Butyl-3-methylimidazolium Hexafluorophosphate by Gas-Liquid Chromatography
- Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
- Solubility of KBr in Binary Solvents Formed by Acetone and Water in the Temperature Range between (288.15 and 313.15) K
- Vapor-Liquid Phase Boundaries of Binary Mixtures of Carbon Dioxide with Ethanol and Acetone
- Solubilities of 1,4-Naphthoquinone in Acetone, Toluene, Xylene, Ethanol, and n-Butyl Alcohol
- Measurement and Correlation of Solubilities of trans-Resveratrol in Ethanol + Water and Acetone + Water Mixed Solvents at Different Temperatures
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
- Solubility of Enrofloxacin Sodium in Various Solvents at Various Temperatures
- Solubilities of Palmitic Acid in Pure Solvents and Its Mixtures
- Solubility of Desmosterol in Five Organic Solvents
- Solubility of Ammonium Thiocyanate in Different Solvents
- Measurement and Correlation for Solubilities of Naphthalene in Acetone, Toluene, Xylene, Ethanol, Heptane, and 1-Butanol
- Solubility of Fluorene in Benzene, Chloroform, Acetone, 1-Propanol, Isobutanol, and Methylbenzene from (283 to 323) K
- Solubility of Acenaphthene in Different Solvents from (283.00 to 323.00) K
- Solubility of Adipic Acid in Acetone, Chloroform, and Toluene
- Solubility of p-Aminobenzenesulfonamide in Supercritical Carbon Dioxide with Acetone Cosolvent
- Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
- Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
- Solubilities of Lauric Acid in n-Hexane, Acetone, Propanol, 2-Propanol, 1-Bromopropane, and Trichloroethylene from (279.0 to 315.3) K
- Solubility of Difloxacin in Acetone, Methanol, and Ethanol from (293.15 to 313.15) K
- Solubility of 2-Aminopyridine in Acetone, Chloroform, and Ethyl Acetate
- Solubility of Deflazacort in Binary Solvent Mixtures
- Solubility of Canthaxanthin in Pure Solvents from (293.15 to 343.15) K
- Solubility of (+)-(S)-2-(6-Methoxynaphthalen-2-yl) Propanoic Acid in Acetone, Methanol, Ethanol, Propan-2-ol, and Ethyl Ethanoate at Temperatures between (278 and 320) K
- Solubility and Metastable Zone of Cefoperazone Sodium in Acetone + Water System
- Solubility of Tiamulin Hydrogen Fumarate in Acetone, Acetonitrile, Ethyl Acetate, Ethyl Formate, and Butyl Acetate from (288.2 to 318.2) K
- Solubility of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Organic Solvents and Solubility of 3-Chlorophthalic Acid and 4-Chlorophthalic Acid in Water from (283.15 to 333.15) K
- Solubilities of 1,1 -(Butane-1,4-diyl)-bis(pyridinium) Dihexafluorophosphate in Acetone + Water from (278.15 to 328.15) K
- Solubility of 3-Aminopyridine in Acetone + n-Butyl Acetate from (288.15 to 323.15) K
- Solubility of Butanedioic Acid in Different Solvents at Temperatures between 283 K and 333 K
- Solubility of p-Aminobenzenesulfonamide in Different Solvents from (283.15 to 323.15) K
- Solubilities of Triadimefon in Acetone + Water from (278.15 to 333.15) K
- Solubility of Fumaric Acid in Propan-2-ol, Ethanol, Acetone, Propan-1-ol, and Water
- Solubility of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
- Solubilities of Methyldiphenylphosphine Oxide in Selected Solvents
- Solubilities of Some Chlorophenols in Supercritical CO2 in the Presence and Absence of Cosolvents
- Solubilities of 3-Pentadecylphenol in Ethanol, 1-Butanol, Toluene, Acetone, Tetrachloromethane, and Ethyl Acetate
- Solubility of Captopril in 2-Propanol, Acetone, Acetonitrile, Methyl Acetate, Ethyl Acetate, and Butyl Acetate
- Solubilities of 3,9-Dimethyl-3,9-dioxide-2,4,8,10-tetraoxa-3,9-diphosphaspiro[5.5]undecane in Selected Solvents
- Solubility of Cytidine 5'-Diphosphocholine Sodium in Water and Different Binary Mixtures from (278.15 to 298.15) K
- Solubilities of 1,1-(Hexane-1,6-diyl)-bis(pyridinium) Dihexafluorophosphate in (Water + Acetone)
- Enthalpies of Solution of 1-Butyl-3-methylimidazolium Tetrafluoroborate in 15 Solvents at 298.15 K
- Density and Viscosity of Ketones with Toluene at Different Temperatures and at Atmospheric Pressure
- Solubilities of 1,1'-(Ethane-1,2-diyl)-bis(pyridinium) Dihexafluorophosphate in Aqueous Acetone Mixtures
- Density and Viscosity of (2,2-Dichloro-N,N-di-2-propenylacetamide + Acetone) and (2,2-Dichloro-N,N-di-2-propenylacetamide + Ethanol) at T = (278.15 to 313.15) K
- Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
- Excess Enthalpies of Dibromomethane with Acetone, 1,4-Dioxane, Pyridine, Diethyl Ether, Ethyl Methyl Ketone, and Tetrahydrofuran at 303.15 K
- Solubility of Camellianin A in Methanol, Acetonitrile, Acetone, and Water from (283.2 to 313.2) K
- Density, Speed of Sound, and Refractive Index of 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate with Acetone, Methyl Acetate, and Ethyl Acetate at Temperatures from (278.15 to 328.15) K
- Experimental Measurement and Correlation of the Solubilities of 2,4-Dichloro-5-methoxypyrimidine in Ethyl Ethanoate, Methanol, Ethanol, Acetone, Tetrachloromethane, and Heptane at Temperatures between (295 and 320) K
- Solubility of 1,1'-(Ethane-1,2-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents
- Solubilities of 1,1?-(Propane-1,3-diyl)-bis(3-methyl-1H-imidazolium-1-yl) Dihexafluorophosphate in Different Solvents
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Henry s Law Constants of Organic Compounds in Water and n-Octane at T = 293.2 K
- Solubilities of (2,5-Dihydroxyphenyl)diphenyl Phosphine Oxide in Selected Solvents
- Solubilities of Sulfadiazine in Methanol, Ethanol, 1-Propanol, 2-Propanol, Acetone, and Chloroform from (294.15 to 318.15) K
- Solubility of Delphinidin in Water and Various Organic Solvents between (298.15 and 343.15) K
- Thermodynamics of Ketone + Amine Mixtures. I. Volumetric and Speed of Sound Data at (293.15, 298.15, and 303.15) K for 2-Propanone + Aniline, + N-Methylaniline, or + Pyridine Systems
- Apparent Molar Volume and Compressibility of Tetrabutylphosphonium Bromide in Various Solvents
- Activity Coefficients at Infinite Dilution Measurements for Organic Solutes and Water in the Ionic Liquid 1-Hexyl-3-methylimidazolium Thiocyanate
- ss-Sitosterol Solubility in Selected Organic Solvents
- Measurement and Modeling of Epigallocatechin Gallate Solubility in Supercritical Carbon Dioxide Fluid with Ethanol Cosolvent
- Solubility of 1,1'-(Butane-1,4-diyl)-bis(3-methylpyridinium) Dihexafluorophosphate in Different Solvents from (288.15 to 333.15) K
- Joback Method
- KDB
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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