- InChI
- InChI=1S/C4H8O2/c1-3-6-4(2)5/h3H2,1-2H3
- InChI Key
- XEKOWRVHYACXOJ-UHFFFAOYSA-N
- Formula
- C4H8O2
- SMILES
- CCOC(C)=O
- Molecular Weight1
- 88.11
- CAS
- 141-78-6
- Other Names
-
- 1-Acetoxyethane
- Acetic acid, ethyl ester
- Acetic ether
- Acetidin
- Acetoxyethane
- Aethylacetat
- CH3COOC2H5
- Essigester
- Ethyl acetic ester
- Ethyl ester of acetic acid
- Ethylacetaat
- Ethyle (acetate d')
- Ethylester kyseliny octove
- Etile (acetato di)
- NSC 70930
- Rcra waste number U112
- UN 1173
- Vinegar naphtha
- ac. acetic ethyl ester
- ethyl ethanoate
- ω : Acentric Factor.
- PAff : Proton affinity (kJ/mol).
- Tig : Autoignition Temperature (K).
- BasG : Gas basicity (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).
- μ : Dipole Moment (debye).
- η : Dynamic viscosity (Pa×s).
- εr : Dielectric Constant (Relative permittivity).
- 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.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Ptriple : Triple Point 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°gas : Molar entropy at standard conditions (J/mol×K).
- S°liquid : Liquid phase molar entropy at standard conditions (J/mol×K).
- csound,fluid : Speed of sound in fluid (m/s).
- γ : Surface Tension (N/m).
- Tboil : Normal Boiling Point Temperature (K).
- Tboil : Boiling point at given pressure (K).
- Tc : Critical Temperature (K).
- λ : Gas thermal conductivity (W/m×K).
- λ : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- UQi : UNIQUAC Qi Parameter.
- URi : UNIQUAC Ri Parameter.
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
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Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | [0.3610; 0.3620] |
|
|
| ω | 0.3610 | ChemSep v8.3 pure component data Compiled value | |
| ω | 0.3620 | KDB | |
| PAff | 835.70 | kJ/mol | NIST |
| Tig | [699.15; 699.82] | K |
|
| Tig | 699.82 | K | KDB |
| Tig | 699.15 | K | NCMS SOLV-DB |
| BasG | [799.90; 804.70] | kJ/mol |
|
| BasG | 804.70 | kJ/mol | NIST |
| BasG | 799.90 ± 0.20 | kJ/mol | NIST |
| ΔcH°liquid | [-2256.00; -2235.40] | kJ/mol |
|
| ΔcH°liquid | -2238.54 ± 0.48 | kJ/mol | NIST |
| ΔcH°liquid | -2235.40 ± 3.90 | kJ/mol | NIST |
| ΔcH°liquid | -2256.00 | kJ/mol | NIST |
| ΔcH°liquid | -2246.00 | kJ/mol | NIST |
| μ | [1.78; 1.90] | debye |
|
| μ | 1.78 | debye | ChemSep v8.3 pure component data Compiled value |
| μ | 1.90 | debye | KDB |
| η | [0.0004260; 0.0004370] | Pa×s |
|
| η | 0.0004370 | Pa×s | A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents |
| η | 0.0004274 | Pa×s | Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents |
| η | 0.0004260 | Pa×s | Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K |
| εr | 6.02 | NCMS SOLV-DB | |
| LFL | 2.20 | % in Air | KDB |
| UFL | 9.00 | % in Air | KDB |
| Tflash,cc | [269.15; 285.93] | K |
|
| Tflash,cc | 285.93 | K | KDB |
| Tflash,cc | 269.15 | K | NCMS SOLV-DB |
| Tflash,oc | 268.71 | K | KDB |
| ΔfG° | [-328.00; -327.60] | kJ/mol |
|
| ΔfG° | -328.00 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfG° | -327.60 | kJ/mol | KDB |
| Rg | 3.3480 | KDB | |
| ΔfH°gas | [-446.90; -443.20] | kJ/mol |
|
| ΔfH°gas | -444.50 | kJ/mol | ChemSep v8.3 pure component data Compiled value |
| ΔfH°gas | -443.20 | kJ/mol | KDB |
| ΔfH°gas | -445.43 ± 0.84 | kJ/mol | NIST |
| ΔfH°gas | -444.80 ± 0.40 | kJ/mol | NIST |
| ΔfH°gas | -443.80 | kJ/mol | NIST |
| ΔfH°gas | -446.90 | kJ/mol | NIST |
| ΔfH°liquid | [-482.00; -478.82] | kJ/mol |
|
| ΔfH°liquid | -480.57 ± 0.79 | kJ/mol | NIST |
| ΔfH°liquid | -479.86 ± 0.46 | kJ/mol | NIST |
| ΔfH°liquid | -478.82 ± 0.73 | kJ/mol | NIST |
| ΔfH°liquid | -482.00 ± 4.00 | kJ/mol | NIST |
| ΔfusH° | 10.48 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.30; 35.69] | kJ/mol |
|
| ΔvapH° | 35.61 | kJ/mol | NCMS SOLV-DB |
| ΔvapH° | 35.69 | kJ/mol | NIST |
| ΔvapH° | 35.00 | kJ/mol | NIST |
| ΔvapH° | 35.10 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 35.10 | kJ/mol | NIST |
| ΔvapH° | 35.60 ± 0.10 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | 35.10 ± 0.20 | kJ/mol | NIST |
| ΔvapH° | Outlier 32.30 ± 0.42 | kJ/mol | NIST |
| IE | [9.90; 10.45] | eV |
|
| IE | 10.01 ± 0.05 | eV | NIST |
| IE | 10.01 ± 0.05 | eV | NIST |
| IE | 10.00 ± 0.10 | eV | NIST |
| IE | 10.16 | eV | NIST |
| IE | 9.90 ± 0.05 | eV | NIST |
| IE | 10.24 | eV | NIST |
| IE | 10.11 ± 0.02 | eV | NIST |
| IE | 10.09 ± 0.02 | eV | NIST |
| IE | Outlier 10.45 | eV | NIST |
| IE | 9.90 | eV | NIST |
| log10WS | [-0.04; -0.04] |
|
|
| log10WS | -0.04 | Aq. Solubility Prediction | |
| log10WS | -0.04 | Estimated Solubility | |
| logPoct/wat | 0.730 | NCMS SOLV-DB | |
| McVol | 74.660 | ml/mol | McGowan Calculated Property |
| NFPA Fire | [%!d(float64=3); %!d(float64=3)] |
|
|
| NFPA Fire | 3 | KDB | |
| NFPA Fire | 3 | NCMS SOLV-DB | |
| NFPA Health | 1 | NCMS SOLV-DB | |
| NFPA Safety | 0 | NCMS SOLV-DB | |
| Pc | [3830.00; 4280.00] | kPa |
|
| Pc | 3900.00 | kPa | Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol |
| Pc | 3830.00 | kPa | ChemSep v8.3 pure component data Compiled value |
| Pc | 3882.00 | kPa | KDB |
| Pc | 3882.00 ± 3.87 | kPa | NIST |
| Pc | 3830.00 ± 81.06 | kPa | NIST |
| Pc | 3851.70 ± 40.00 | kPa | NIST |
| Pc | 4018.00 ± 202.65 | kPa | NIST |
| Pc | Outlier 4280.00 ± 405.30 | kPa | NIST |
| Ptriple | 1.43e-03 | kPa | ChemSep v8.3 pure component data Compiled value |
| ρc | [299.29; 308.10] | kg/m3 |
|
| ρc | 307.66 ± 5.29 | kg/m3 | NIST |
| ρc | 308.10 ± 4.41 | kg/m3 | NIST |
| ρc | 299.29 ± 5.29 | kg/m3 | NIST |
| Inp | [554.00; 634.00] |
|
|
| Inp | 611.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | Outlier 568.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 578.95 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 609.70 | NIST | |
| Inp | 604.40 | NIST | |
| Inp | 611.70 | NIST | |
| Inp | 605.10 | NIST | |
| Inp | 600.80 | NIST | |
| Inp | 599.30 | NIST | |
| Inp | 597.30 | NIST | |
| Inp | Outlier 563.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 607.50 | NIST | |
| Inp | 605.70 | NIST | |
| Inp | 602.40 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | Outlier 572.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | Outlier 567.00 | NIST | |
| Inp | 595.70 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | Outlier 571.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 618.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 579.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 577.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 609.10 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 599.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 581.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 626.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 617.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 599.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 624.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 623.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | Outlier 628.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 591.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | Outlier 554.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 606.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | Outlier 628.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 608.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | Outlier 628.00 | NIST | |
| Inp | Outlier 628.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | Outlier 630.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 601.82 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 597.00 | NIST | |
| Inp | 588.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 583.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | Outlier 568.00 | NIST | |
| Inp | 580.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 594.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 610.00 | NIST | |
| Inp | Outlier 633.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 599.00 | NIST | |
| Inp | Outlier 628.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 584.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | Outlier 634.00 | NIST | |
| Inp | 605.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 612.00 | NIST | |
| Inp | 621.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 613.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 592.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 609.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 620.00 | NIST | |
| Inp | 590.00 | NIST | |
| Inp | 615.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 602.00 | NIST | |
| Inp | 604.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 593.00 | NIST | |
| Inp | 600.00 | NIST | |
| Inp | 611.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 607.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 589.00 | NIST | |
| Inp | Outlier 633.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 596.00 | NIST | |
| I | [850.00; 921.00] |
|
|
| I | 902.00 | NIST | |
| I | 875.00 | NIST | |
| I | 908.00 | NIST | |
| I | 881.00 | NIST | |
| I | 880.00 | NIST | |
| I | 906.00 | NIST | |
| I | 898.00 | NIST | |
| I | 890.00 | NIST | |
| I | 885.00 | NIST | |
| I | 884.00 | NIST | |
| I | 887.00 | NIST | |
| I | 906.00 | NIST | |
| I | 874.00 | NIST | |
| I | 880.00 | NIST | |
| I | 880.00 | NIST | |
| I | 870.00 | NIST | |
| I | Outlier 856.00 | NIST | |
| I | Outlier 858.00 | NIST | |
| I | 882.00 | NIST | |
| I | 889.00 | NIST | |
| I | 895.00 | NIST | |
| I | 900.00 | NIST | |
| I | Outlier 917.00 | NIST | |
| I | 896.00 | NIST | |
| I | 889.00 | NIST | |
| I | 891.00 | NIST | |
| I | 894.00 | NIST | |
| I | 889.00 | NIST | |
| I | 900.00 | NIST | |
| I | 886.00 | NIST | |
| I | 914.00 | NIST | |
| I | 890.00 | NIST | |
| I | 908.00 | NIST | |
| I | 893.00 | NIST | |
| I | 878.00 | NIST | |
| I | 900.00 | NIST | |
| I | 898.00 | NIST | |
| I | 893.00 | NIST | |
| I | 870.00 | NIST | |
| I | 901.00 | NIST | |
| I | 904.00 | NIST | |
| I | 901.00 | NIST | |
| I | 880.00 | NIST | |
| I | 894.00 | NIST | |
| I | 870.00 | NIST | |
| I | 891.00 | NIST | |
| I | 863.00 | NIST | |
| I | 891.00 | NIST | |
| I | 882.00 | NIST | |
| I | 863.00 | NIST | |
| I | 887.00 | NIST | |
| I | 888.00 | NIST | |
| I | 888.00 | NIST | |
| I | 890.00 | NIST | |
| I | 907.00 | NIST | |
| I | 902.00 | NIST | |
| I | 885.00 | NIST | |
| I | 884.00 | NIST | |
| I | 870.00 | NIST | |
| I | 870.00 | NIST | |
| I | 872.00 | NIST | |
| I | 867.00 | NIST | |
| I | 867.00 | NIST | |
| I | 881.00 | NIST | |
| I | 890.00 | NIST | |
| I | 893.00 | NIST | |
| I | Outlier 854.00 | NIST | |
| I | 882.00 | NIST | |
| I | 892.00 | NIST | |
| I | 881.00 | NIST | |
| I | 866.00 | NIST | |
| I | 899.00 | NIST | |
| I | 893.00 | NIST | |
| I | 891.00 | NIST | |
| I | 899.00 | NIST | |
| I | 896.00 | NIST | |
| I | 872.00 | NIST | |
| I | 874.00 | NIST | |
| I | 904.00 | NIST | |
| I | 900.00 | NIST | |
| I | 892.00 | NIST | |
| I | 888.00 | NIST | |
| I | 912.40 | NIST | |
| I | 900.00 | NIST | |
| I | 868.00 | NIST | |
| I | 880.00 | NIST | |
| I | 908.00 | NIST | |
| I | 878.00 | NIST | |
| I | 903.00 | NIST | |
| I | 898.00 | NIST | |
| I | 885.00 | NIST | |
| I | 890.00 | NIST | |
| I | 904.00 | NIST | |
| I | 877.00 | NIST | |
| I | 892.00 | NIST | |
| I | 892.00 | NIST | |
| I | 900.00 | NIST | |
| I | 892.00 | NIST | |
| I | 891.00 | NIST | |
| I | 889.00 | NIST | |
| I | 900.00 | NIST | |
| I | 905.00 | NIST | |
| I | 872.00 | NIST | |
| I | 900.00 | NIST | |
| I | 899.00 | NIST | |
| I | 890.00 | NIST | |
| I | 890.00 | NIST | |
| I | Outlier 856.00 | NIST | |
| I | 885.00 | NIST | |
| I | 891.00 | NIST | |
| I | 901.00 | NIST | |
| I | 892.00 | NIST | |
| I | 890.00 | NIST | |
| I | 903.00 | NIST | |
| I | Outlier 921.00 | NIST | |
| I | 882.00 | NIST | |
| I | 893.00 | NIST | |
| I | Outlier 850.00 | NIST | |
| I | 884.00 | NIST | |
| I | 889.00 | NIST | |
| I | Outlier 920.00 | NIST | |
| I | 890.00 | NIST | |
| I | 885.00 | NIST | |
| I | Outlier 850.00 | NIST | |
| I | Outlier 850.00 | NIST | |
| I | 861.00 | NIST | |
| I | 870.00 | NIST | |
| I | 882.00 | NIST | |
| I | 894.00 | NIST | |
| I | 883.00 | NIST | |
| I | 885.00 | NIST | |
| I | 908.00 | NIST | |
| I | Outlier 854.00 | NIST | |
| I | 878.00 | NIST | |
| I | 890.00 | NIST | |
| I | 877.00 | NIST | |
| I | 882.00 | NIST | |
| I | 912.00 | NIST | |
| I | 885.00 | NIST | |
| I | 872.70 | NIST | |
| I | 872.00 | NIST | |
| I | 882.00 | NIST | |
| I | 882.00 | NIST | |
| I | 877.00 | NIST | |
| I | 879.00 | NIST | |
| I | 886.00 | NIST | |
| I | 887.00 | NIST | |
| I | 889.00 | NIST | |
| I | 889.00 | NIST | |
| I | 890.00 | NIST | |
| I | 890.00 | NIST | |
| I | 872.00 | NIST | |
| I | 880.00 | NIST | |
| I | 888.00 | NIST | |
| I | 891.00 | NIST | |
| I | 880.00 | NIST | |
| I | 872.00 | NIST | |
| I | 880.00 | NIST | |
| I | 883.00 | NIST | |
| I | 882.00 | NIST | |
| I | Outlier 857.00 | NIST | |
| I | Outlier 858.00 | NIST | |
| I | 862.00 | NIST | |
| I | 907.00 | NIST | |
| I | 870.00 | NIST | |
| I | 885.00 | NIST | |
| I | 870.00 | NIST | |
| I | Outlier 915.00 | NIST | |
| I | 894.00 | NIST | |
| I | 896.00 | NIST | |
| I | 909.00 | NIST | |
| I | 895.00 | NIST | |
| I | 892.00 | NIST | |
| I | 861.00 | NIST | |
| I | 882.00 | NIST | |
| I | 885.00 | NIST | |
| I | 871.00 | NIST | |
| I | 885.00 | NIST | |
| I | 885.00 | NIST | |
| I | 891.00 | NIST | |
| I | 893.00 | NIST | |
| I | 897.00 | NIST | |
| I | 872.00 | NIST | |
| I | 898.00 | NIST | |
| I | 885.00 | NIST | |
| I | 898.00 | NIST | |
| I | 878.00 | NIST | |
| I | 885.00 | NIST | |
| I | 868.00 | NIST | |
| I | 866.00 | NIST | |
| I | 866.00 | NIST | |
| I | 898.00 | NIST | |
| I | Outlier 853.00 | NIST | |
| I | 898.00 | NIST | |
| I | 898.00 | NIST | |
| I | 891.00 | NIST | |
| I | 885.00 | NIST | |
| I | 893.00 | NIST | |
| I | 872.00 | NIST | |
| I | 898.00 | NIST | |
| I | 900.00 | NIST | |
| I | 893.00 | NIST | |
| I | 893.00 | NIST | |
| I | 872.00 | NIST | |
| I | 895.00 | NIST | |
| I | 895.00 | NIST | |
| I | 886.00 | NIST | |
| I | 895.00 | NIST | |
| I | 900.00 | NIST | |
| I | 872.00 | NIST | |
| I | 888.00 | NIST | |
| I | 888.00 | NIST | |
| I | 900.00 | NIST | |
| I | 882.00 | NIST | |
| I | 882.00 | NIST | |
| I | 873.00 | NIST | |
| I | 872.00 | NIST | |
| I | 872.00 | NIST | |
| I | 886.00 | NIST | |
| I | 889.00 | NIST | |
| I | 906.00 | NIST | |
| I | 870.00 | NIST | |
| I | 872.00 | NIST | |
| I | 890.00 | NIST | |
| I | 874.00 | NIST | |
| I | Outlier 858.00 | NIST | |
| I | Outlier 917.00 | NIST | |
| I | 896.00 | NIST | |
| I | 900.00 | NIST | |
| I | 893.00 | NIST | |
| I | 870.00 | NIST | |
| I | 894.00 | NIST | |
| I | 882.00 | NIST | |
| I | 881.00 | NIST | |
| I | 892.00 | NIST | |
| S°gas | 362.75 | J/mol×K | NIST |
| S°liquid | 259.40 | J/mol×K | NIST |
| Tboil | [346.65; 375.00] | K |
|
| Tboil | 350.27 | K | Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa |
| Tboil | 350.24 | K | Vapor liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa |
| Tboil | 350.24 | K | Liquid-liquid equilibria of water + 3-hydroxy-2-butanone + ethyl ethanoate |
| Tboil | 350.20 | K | Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model |
| Tboil | 350.15 | K | The isobaric vapor liquid equilibria of ethyl acetate p acetonitrile p bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa |
| Tboil | 350.29 | K | Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate + propyl acetate + dimethyl sulfoxide and binary systems of ethyl acetate + dimethyl sulfoxide and propyl acetate + dimethyl sulfoxide at 101.3 kPa |
| Tboil | 350.35 | K | Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa |
| Tboil | 350.16 | K | Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil |
| Tboil | 350.20 | K | Isobaric Vapor Liquid Equilibrium for Three Binary Systems of Acetaldehyde + Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa |
| Tboil | 349.95 | K | Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa |
| Tboil | 350.28 | K | Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa |
| Tboil | 350.25 | K | Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing |
| Tboil | 350.15 | K | Vapor-Liquid Equilibrium of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa |
| Tboil | 350.21 | K | Volumetric Behavior and Saturated Pressure for Carbon Dioxide + Ethyl Acetate at a Temperature of 313.15 K |
| Tboil | 350.15 | K | Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10) |
| Tboil | 350.19 | K | Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa |
| Tboil | 350.21 | K | ChemSep v8.3 pure component data Compiled value |
| Tboil | 350.26 | K | KDB |
| Tboil | 350.21 | K | NCMS SOLV-DB |
| Tboil | 350.13 ± 0.30 | K | NIST |
| Tboil | 350.20 | K | NIST |
| Tboil | 350.00 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 349.25 ± 0.30 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.30 ± 0.20 | K | NIST |
| Tboil | 350.30 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.19 ± 0.50 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.30 ± 0.20 | K | NIST |
| Tboil | 350.30 ± 0.30 | K | NIST |
| Tboil | Outlier 375.00 ± 2.00 | K | NIST |
| Tboil | 350.35 | K | NIST |
| Tboil | 350.05 ± 0.30 | K | NIST |
| Tboil | 350.21 ± 0.50 | K | NIST |
| Tboil | 350.25 ± 0.50 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.00 ± 2.00 | K | NIST |
| Tboil | 350.29 ± 0.15 | K | NIST |
| Tboil | 350.15 ± 2.00 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.25 ± 0.50 | K | NIST |
| Tboil | 350.25 ± 0.30 | K | NIST |
| Tboil | 350.65 ± 2.00 | K | NIST |
| Tboil | 349.65 ± 2.00 | K | NIST |
| Tboil | 352.15 ± 2.00 | K | NIST |
| Tboil | 350.25 ± 1.00 | K | NIST |
| Tboil | 350.30 ± 1.00 | K | NIST |
| Tboil | 350.30 ± 1.00 | K | NIST |
| Tboil | 349.97 ± 2.00 | K | NIST |
| Tboil | 351.15 ± 2.00 | K | NIST |
| Tboil | 350.45 ± 1.00 | K | NIST |
| Tboil | 350.25 ± 1.00 | K | NIST |
| Tboil | 350.30 ± 0.40 | K | NIST |
| Tboil | 349.15 ± 2.00 | K | NIST |
| Tboil | 349.65 ± 2.50 | K | NIST |
| Tboil | 350.26 ± 0.06 | K | NIST |
| Tboil | 350.30 ± 0.15 | K | NIST |
| Tboil | 350.00 ± 2.00 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.15 ± 2.00 | K | NIST |
| Tboil | 349.95 ± 2.00 | K | NIST |
| Tboil | 350.20 ± 0.50 | K | NIST |
| Tboil | 350.30 ± 0.20 | K | NIST |
| Tboil | 350.25 ± 0.50 | K | NIST |
| Tboil | 350.21 ± 0.50 | K | NIST |
| Tboil | 349.65 ± 2.00 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.45 ± 0.60 | K | NIST |
| Tboil | 350.30 ± 0.30 | K | NIST |
| Tboil | 350.25 ± 1.00 | K | NIST |
| Tboil | 350.30 ± 0.20 | K | NIST |
| Tboil | 350.25 ± 1.00 | K | NIST |
| Tboil | 349.90 ± 0.20 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.30 ± 0.20 | K | NIST |
| Tboil | 350.30 ± 0.50 | K | NIST |
| Tboil | 350.30 ± 2.00 | K | NIST |
| Tboil | 350.20 ± 2.00 | K | NIST |
| Tboil | 350.30 ± 2.00 | K | NIST |
| Tboil | 350.10 ± 2.00 | K | NIST |
| Tboil | 350.70 ± 2.00 | K | NIST |
| Tboil | 350.65 ± 2.00 | K | NIST |
| Tboil | 346.65 ± 3.00 | K | NIST |
| Tboil | 347.45 ± 2.00 | K | NIST |
| Tboil | 347.45 ± 2.00 | K | NIST |
| Tc | [513.00; 548.90] | K |
|
| Tc | 523.29 | K | Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements |
| Tc | 523.20 | K | ChemSep v8.3 pure component data Compiled value |
| Tc | 523.30 | K | KDB |
| Tc | 523.20 | K | NIST |
| Tc | 523.30 ± 0.05 | K | NIST |
| Tc | 523.30 ± 1.00 | K | NIST |
| Tc | 523.30 ± 1.00 | K | NIST |
| Tc | Outlier 548.90 ± 20.00 | K | NIST |
| Tc | 522.70 ± 2.00 | K | NIST |
| Tc | 513.00 ± 6.00 | K | NIST |
| Tfus | [189.18; 190.77] | K |
|
| Tfus | 189.60 | K | ChemSep v8.3 pure component data Compiled value |
| Tfus | 189.50 | K | KDB |
| Tfus | 189.25 | K | Aq. Solubility Prediction |
| Tfus | 189.55 | K | NCMS SOLV-DB |
| Tfus | 189.55 | K | NIST |
| Tfus | 189.18 ± 0.05 | K | NIST |
| Tfus | 189.35 ± 0.30 | K | NIST |
| Tfus | 189.55 ± 0.10 | K | NIST |
| Tfus | 189.77 ± 0.30 | K | NIST |
| Tfus | Outlier 190.77 ± 0.20 | K | NIST |
| Tfus | 190.00 ± 2.00 | K | NIST |
| Ttriple | [189.30; 189.60] | K |
|
| Ttriple | 189.60 | K | ChemSep v8.3 pure component data Compiled value |
| Ttriple | 189.30 ± 0.05 | K | NIST |
| Ttriple | 189.30 ± 0.20 | K | NIST |
| Ttriple | 189.30 ± 0.20 | K | NIST |
| UQi | 3.12 | ChemSep v8.3 pure component data Compiled value | |
| URi | 3.48 | ChemSep v8.3 pure component data Compiled value | |
| Vc | [0.286; 0.286] | m3/kmol |
|
| Vc | 0.286 | m3/kmol | ChemSep v8.3 pure component data Compiled value |
| Vc | 0.286 | m3/kmol | KDB |
| Zc | [0.2520000; 0.2551730] |
|
|
| Zc | 0.2520000 | ChemSep v8.3 pure component data Compiled value | |
| Zc | 0.2551730 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
Pressure Dependent Properties
Datasets
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Temperature, K - Liquid | Pressure, kPa - Liquid | Mass density, kg/m3 - Liquid |
| 298.15 | 100.00 | 894.0 |
| 298.15 | 1000.00 | 894.7 |
| 298.15 | 2000.00 | 895.7 |
| 298.15 | 3000.00 | 896.7 |
| 298.15 | 3800.00 | 897.4 |
| 298.15 | 5000.00 | 898.8 |
| 298.15 | 10000.00 | 903.4 |
| 298.15 | 15000.00 | 907.7 |
| 298.15 | 20000.00 | 912.0 |
| 298.15 | 25000.00 | 916.1 |
| 298.15 | 30000.00 | 921.1 |
| 298.15 | 35000.00 | 926.3 |
| 303.15 | 100.00 | 887.6 |
| 303.15 | 1000.00 | 888.5 |
| 303.15 | 2000.00 | 889.5 |
| 303.15 | 3000.00 | 890.5 |
| 303.15 | 3800.00 | 891.3 |
| 303.15 | 5000.00 | 892.7 |
| 303.15 | 10000.00 | 897.5 |
| 303.15 | 15000.00 | 902.0 |
| 303.15 | 20000.00 | 906.3 |
| 303.15 | 25000.00 | 910.7 |
| 303.15 | 30000.00 | 915.9 |
| 303.15 | 35000.00 | 921.2 |
| 308.15 | 100.00 | 881.4 |
| 308.15 | 1000.00 | 882.3 |
| 308.15 | 2000.00 | 883.3 |
| 308.15 | 3000.00 | 884.4 |
| 308.15 | 3800.00 | 885.3 |
| 308.15 | 5000.00 | 886.7 |
| 308.15 | 10000.00 | 891.7 |
| 308.15 | 15000.00 | 896.4 |
| 308.15 | 20000.00 | 900.9 |
| 308.15 | 25000.00 | 905.4 |
| 308.15 | 30000.00 | 910.7 |
| 308.15 | 35000.00 | 916.2 |
| 313.15 | 100.00 | 875.2 |
| 313.15 | 1000.00 | 876.1 |
| 313.15 | 2000.00 | 877.2 |
| 313.15 | 3000.00 | 878.3 |
| 313.15 | 3800.00 | 879.2 |
| 313.15 | 5000.00 | 880.6 |
| 313.15 | 10000.00 | 885.8 |
| 313.15 | 15000.00 | 890.7 |
| 313.15 | 20000.00 | 895.4 |
| 313.15 | 25000.00 | 899.8 |
| 313.15 | 30000.00 | 905.3 |
| 313.15 | 35000.00 | 910.9 |
| 318.15 | 100.00 | 868.8 |
| 318.15 | 1000.00 | 869.8 |
| 318.15 | 2000.00 | 871.0 |
| 318.15 | 3000.00 | 872.2 |
| 318.15 | 3800.00 | 873.1 |
| 318.15 | 5000.00 | 874.5 |
| 318.15 | 10000.00 | 880.0 |
| 318.15 | 15000.00 | 885.1 |
| 318.15 | 20000.00 | 889.8 |
| 318.15 | 25000.00 | 894.5 |
| 318.15 | 30000.00 | 900.1 |
| 318.15 | 35000.00 | 905.9 |
| 323.15 | 100.00 | 862.7 |
| 323.15 | 1000.00 | 864.0 |
| 323.15 | 2000.00 | 865.1 |
| 323.15 | 3000.00 | 866.2 |
| 323.15 | 3800.00 | 867.1 |
| 323.15 | 5000.00 | 868.6 |
| 323.15 | 10000.00 | 874.2 |
| 323.15 | 15000.00 | 879.4 |
| 323.15 | 20000.00 | 884.3 |
| 323.15 | 25000.00 | 889.2 |
| 323.15 | 30000.00 | 895.0 |
| 323.15 | 35000.00 | 900.9 |
| 328.15 | 100.00 | 856.4 |
| 328.15 | 1000.00 | 857.8 |
| 328.15 | 2000.00 | 859.2 |
| 328.15 | 3000.00 | 860.5 |
| 328.15 | 3800.00 | 861.5 |
| 328.15 | 5000.00 | 862.5 |
| 328.15 | 10000.00 | 868.4 |
| 328.15 | 15000.00 | 873.9 |
| 328.15 | 20000.00 | 879.0 |
| 328.15 | 25000.00 | 884.1 |
| 328.15 | 30000.00 | 890.1 |
| 328.15 | 35000.00 | 896.2 |
| 333.15 | 100.00 | 850.4 |
| 333.15 | 1000.00 | 851.7 |
| 333.15 | 2000.00 | 853.0 |
| 333.15 | 3000.00 | 854.4 |
| 333.15 | 3800.00 | 855.4 |
| 333.15 | 5000.00 | 856.8 |
| 333.15 | 10000.00 | 862.9 |
| 333.15 | 15000.00 | 868.5 |
| 333.15 | 20000.00 | 873.8 |
| 333.15 | 25000.00 | 879.0 |
| 333.15 | 30000.00 | 885.2 |
| 333.15 | 35000.00 | 891.4 |
| 338.15 | 100.00 | 844.0 |
| 338.15 | 1000.00 | 845.4 |
| 338.15 | 2000.00 | 846.8 |
| 338.15 | 3000.00 | 848.2 |
| 338.15 | 3800.00 | 849.3 |
| 338.15 | 5000.00 | 850.8 |
| 338.15 | 10000.00 | 857.1 |
| 338.15 | 15000.00 | 863.0 |
| 338.15 | 20000.00 | 868.5 |
| 338.15 | 25000.00 | 873.9 |
| 338.15 | 30000.00 | 880.3 |
| 338.15 | 35000.00 | 886.7 |
| 343.15 | 100.00 | 837.5 |
| 343.15 | 1000.00 | 839.1 |
| 343.15 | 2000.00 | 840.6 |
| 343.15 | 3000.00 | 842.0 |
| 343.15 | 3800.00 | 843.2 |
| 343.15 | 5000.00 | 844.5 |
| 343.15 | 10000.00 | 851.2 |
| 343.15 | 15000.00 | 857.3 |
| 343.15 | 20000.00 | 863.0 |
| 343.15 | 25000.00 | 868.5 |
| 343.15 | 30000.00 | 875.1 |
| 343.15 | 35000.00 | 881.6 |
| 348.15 | 100.00 | 829.4 |
| 348.15 | 1000.00 | 830.5 |
| 348.15 | 2000.00 | 832.3 |
| 348.15 | 3000.00 | 833.8 |
| 348.15 | 3800.00 | 835.0 |
| 348.15 | 5000.00 | 836.8 |
| 348.15 | 10000.00 | 845.5 |
| 348.15 | 15000.00 | 851.8 |
| 348.15 | 20000.00 | 857.7 |
| 348.15 | 25000.00 | 863.5 |
| 348.15 | 30000.00 | 870.2 |
| 348.15 | 35000.00 | 877.0 |
| 353.15 | 1000.00 | 824.3 |
| 353.15 | 2000.00 | 826.0 |
| 353.15 | 3000.00 | 827.5 |
| 353.15 | 3800.00 | 828.8 |
| 353.15 | 5000.00 | 830.6 |
| 353.15 | 10000.00 | 837.7 |
| 353.15 | 15000.00 | 844.3 |
| 353.15 | 20000.00 | 850.4 |
| 353.15 | 25000.00 | 856.1 |
| 353.15 | 30000.00 | 862.7 |
| 353.15 | 35000.00 | 869.6 |
| 358.15 | 1000.00 | 818.4 |
| 358.15 | 2000.00 | 820.0 |
| 358.15 | 3000.00 | 821.6 |
| 358.15 | 3800.00 | 822.8 |
| 358.15 | 5000.00 | 824.7 |
| 358.15 | 10000.00 | 832.1 |
| 358.15 | 15000.00 | 838.9 |
| 358.15 | 20000.00 | 845.2 |
| 358.15 | 25000.00 | 851.0 |
| 358.15 | 30000.00 | 857.6 |
| 358.15 | 35000.00 | 864.7 |
| 363.15 | 1000.00 | 811.8 |
| 363.15 | 2000.00 | 813.5 |
| 363.15 | 3000.00 | 815.3 |
| 363.15 | 3800.00 | 816.6 |
| 363.15 | 5000.00 | 818.5 |
| 363.15 | 10000.00 | 826.3 |
| 363.15 | 15000.00 | 833.3 |
| 363.15 | 20000.00 | 839.7 |
| 363.15 | 25000.00 | 845.8 |
| 363.15 | 30000.00 | 852.9 |
| 363.15 | 35000.00 | 860.2 |
| 368.15 | 1000.00 | 804.9 |
| 368.15 | 2000.00 | 806.8 |
| 368.15 | 3000.00 | 808.6 |
| 368.15 | 3800.00 | 810.0 |
| 368.15 | 5000.00 | 812.1 |
| 368.15 | 10000.00 | 820.2 |
| 368.15 | 15000.00 | 827.5 |
| 368.15 | 20000.00 | 834.3 |
| 368.15 | 25000.00 | 840.6 |
| 368.15 | 30000.00 | 848.0 |
| 368.15 | 35000.00 | 855.5 |
| 373.15 | 1000.00 | 798.5 |
| 373.15 | 2000.00 | 800.4 |
| 373.15 | 3000.00 | 802.4 |
| 373.15 | 3800.00 | 803.8 |
| 373.15 | 5000.00 | 806.0 |
| 373.15 | 10000.00 | 814.4 |
| 373.15 | 15000.00 | 822.0 |
| 373.15 | 20000.00 | 829.0 |
| 373.15 | 25000.00 | 835.5 |
| 373.15 | 30000.00 | 843.0 |
| 373.15 | 35000.00 | 850.6 |
| 378.15 | 1000.00 | 791.8 |
| 378.15 | 2000.00 | 793.8 |
| 378.15 | 3000.00 | 795.8 |
| 378.15 | 3800.00 | 797.3 |
| 378.15 | 5000.00 | 799.6 |
| 378.15 | 10000.00 | 808.5 |
| 378.15 | 15000.00 | 816.5 |
| 378.15 | 20000.00 | 823.7 |
| 378.15 | 25000.00 | 830.5 |
| 378.15 | 30000.00 | 838.4 |
| 378.15 | 35000.00 | 846.3 |
| 383.15 | 1000.00 | 784.8 |
| 383.15 | 2000.00 | 787.1 |
| 383.15 | 3000.00 | 789.1 |
| 383.15 | 3800.00 | 790.8 |
| 383.15 | 5000.00 | 793.2 |
| 383.15 | 10000.00 | 802.4 |
| 383.15 | 15000.00 | 810.7 |
| 383.15 | 20000.00 | 818.2 |
| 383.15 | 25000.00 | 825.3 |
| 383.15 | 30000.00 | 833.5 |
| 383.15 | 35000.00 | 841.6 |
| 388.15 | 1000.00 | 778.2 |
| 388.15 | 2000.00 | 780.5 |
| 388.15 | 3000.00 | 782.7 |
| 388.15 | 3800.00 | 784.4 |
| 388.15 | 5000.00 | 786.9 |
| 388.15 | 10000.00 | 796.4 |
| 388.15 | 15000.00 | 805.1 |
| 388.15 | 20000.00 | 813.0 |
| 388.15 | 25000.00 | 820.3 |
| 388.15 | 30000.00 | 828.8 |
| 388.15 | 35000.00 | 837.2 |
| 393.15 | 1000.00 | 771.0 |
| 393.15 | 2000.00 | 773.5 |
| 393.15 | 3000.00 | 775.9 |
| 393.15 | 3800.00 | 777.7 |
| 393.15 | 5000.00 | 780.4 |
| 393.15 | 10000.00 | 790.5 |
| 393.15 | 15000.00 | 799.4 |
| 393.15 | 20000.00 | 807.6 |
| 393.15 | 25000.00 | 815.2 |
| 393.15 | 30000.00 | 823.9 |
| 393.15 | 35000.00 | 832.4 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [100.13; 266.84] | J/mol×K | [200.00; 1500.00] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,gas in J/mol×K, T in K | |||
| Coefficient A | 9.71830e+01 | |||
| Coefficient B | -1.12140e+03 | |||
| Coefficient C | 6.91924e+00 | |||
| Coefficient D | -1.23430e-03 | |||
| Coefficient E | 3.61580e-07 | |||
| Comment | ChemSep eq 16, IdealGasHeatCapacityCp | |||
| Temperature range, min. | 200.00 | |||
| Temperature range, max. | 1500.00 | |||
| Cp,gas | 100.13 | J/mol×K | 200.00 | Calculated Property |
| Cp,gas | 123.79 | J/mol×K | 344.44 | Calculated Property |
| Cp,gas | 158.04 | J/mol×K | 488.89 | Calculated Property |
| Cp,gas | 188.28 | J/mol×K | 633.33 | Calculated Property |
| Cp,gas | 211.18 | J/mol×K | 777.78 | Calculated Property |
| Cp,gas | 227.83 | J/mol×K | 922.22 | Calculated Property |
| Cp,gas | 240.17 | J/mol×K | 1066.67 | Calculated Property |
| Cp,gas | 249.93 | J/mol×K | 1211.11 | Calculated Property |
| Cp,gas | 258.48 | J/mol×K | 1355.56 | Calculated Property |
| Cp,gas | 266.84 | J/mol×K | 1500.00 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,liquid | [162.57; 197.54] | J/mol×K | [189.30; 391.65] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is Cp,liquid in J/mol×K, T in K | |||
| Coefficient A | 1.29430e+02 | |||
| Coefficient B | 9.61920e+02 | |||
| Coefficient C | -7.03470e+00 | |||
| Coefficient D | 3.47450e-02 | |||
| Coefficient E | -3.13460e-05 | |||
| Comment | ChemSep eq 16, LiquidHeatCapacityCp | |||
| Temperature range, min. | 189.30 | |||
| Temperature range, max. | 391.65 | |||
| Cp,liquid | 162.57 | J/mol×K | 189.30 | Calculated Property |
| Cp,liquid | 161.24 | J/mol×K | 211.78 | Calculated Property |
| Cp,liquid | 162.24 | J/mol×K | 234.27 | Calculated Property |
| Cp,liquid | 164.81 | J/mol×K | 256.75 | Calculated Property |
| Cp,liquid | 168.61 | J/mol×K | 279.23 | Calculated Property |
| Cp,liquid | 173.38 | J/mol×K | 301.72 | Calculated Property |
| Cp,liquid | 178.93 | J/mol×K | 324.20 | Calculated Property |
| Cp,liquid | 185.02 | J/mol×K | 346.68 | Calculated Property |
| Cp,liquid | 191.34 | J/mol×K | 369.17 | Calculated Property |
| Cp,liquid | 197.54 | J/mol×K | 391.65 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| η | [0.0011331; 0.0000913] | Pa×s | [220.00; 473.15] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is η in Pa×s, T in K | |||
| Coefficient A | 1.64280e+01 | |||
| Coefficient B | -2.19290e+02 | |||
| Coefficient C | -4.12400e+00 | |||
| Coefficient D | 6.05680e-07 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, LiquidViscosity | |||
| Temperature range, min. | 220.00 | |||
| Temperature range, max. | 473.15 | |||
| η | 0.0011331 | Pa×s | 220.00 | Calculated Property |
| η | 0.0007786 | Pa×s | 248.13 | Calculated Property |
| η | 0.0005520 | Pa×s | 276.26 | Calculated Property |
| η | 0.0004022 | Pa×s | 304.38 | Calculated Property |
| η | 0.0003001 | Pa×s | 332.51 | Calculated Property |
| η | 0.0002287 | Pa×s | 360.64 | Calculated Property |
| η | 0.0001776 | Pa×s | 388.77 | Calculated Property |
| η | 0.0001402 | Pa×s | 416.89 | Calculated Property |
| η | 0.0001124 | Pa×s | 445.02 | Calculated Property |
| η | 0.0000913 | Pa×s | 473.15 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ΔvapH | [41.61; 13.43] | kJ/mol | [189.60; 505.74] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·(1 − Tr)^(B + C·Tr + D·Tr² + E·Tr³), Tr = T/Tc Y is ΔvapH in kJ/mol, T in K | |||
| Coefficient A | 4.95270e+01 | |||
| Coefficient B | 3.70290e-01 | |||
| Coefficient C | 7.26850e-02 | |||
| Coefficient D | -7.74930e-02 | |||
| Coefficient E | 1.73810e-02 | |||
| Critical temperature, Tc (K) | 5.23200e+02 | |||
| Comment | ChemSep eq 106, HeatOfVaporization | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 505.74 | |||
| ΔvapH | 41.61 | kJ/mol | 189.60 | Calculated Property |
| ΔvapH | 39.82 | kJ/mol | 224.73 | Calculated Property |
| ΔvapH | 37.91 | kJ/mol | 259.85 | Calculated Property |
| ΔvapH | 35.84 | kJ/mol | 294.98 | Calculated Property |
| ΔvapH | 33.59 | kJ/mol | 330.11 | Calculated Property |
| ΔvapH | 31.08 | kJ/mol | 365.23 | Calculated Property |
| ΔvapH | 28.21 | kJ/mol | 400.36 | Calculated Property |
| ΔvapH | 24.81 | kJ/mol | 435.49 | Calculated Property |
| ΔvapH | 20.42 | kJ/mol | 470.61 | Calculated Property |
| ΔvapH | 13.43 | kJ/mol | 505.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [258.37; 372.76] |
The Yaws Handbook of Vapor Pressure
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.47020e+01 | |||
| Coefficient B | -3.08216e+03 | |||
| Coefficient C | -4.45420e+01 | |||
| Temperature range, min. | 258.37 | |||
| Temperature range, max. | 372.76 | |||
| Pvap | 1.33 | kPa | 258.37 | Calculated Property |
| Pvap | 2.99 | kPa | 271.08 | Calculated Property |
| Pvap | 6.17 | kPa | 283.79 | Calculated Property |
| Pvap | 11.81 | kPa | 296.50 | Calculated Property |
| Pvap | 21.26 | kPa | 309.21 | Calculated Property |
| Pvap | 36.24 | kPa | 321.92 | Calculated Property |
| Pvap | 58.97 | kPa | 334.63 | Calculated Property |
| Pvap | 92.12 | kPa | 347.34 | Calculated Property |
| Pvap | 138.81 | kPa | 360.05 | Calculated Property |
| Pvap | 202.64 | kPa | 372.76 | Calculated Property |
| Pvap | [1.28e-03; 3819.89] | kPa | [189.60; 523.30] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = exp(A + B/T + C·ln(T) + D·T^E) Y is Pvap in kPa, T in K | |||
| Coefficient A | 8.62609e+01 | |||
| Coefficient B | -7.07329e+03 | |||
| Coefficient C | -1.06598e+01 | |||
| Coefficient D | 8.16528e-06 | |||
| Coefficient E | 2.00000e+00 | |||
| Comment | ChemSep eq 101, VaporPressure | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 523.30 | |||
| Pvap | 1.28e-03 | kPa | 189.60 | Calculated Property |
| Pvap | 0.10 | kPa | 226.68 | Calculated Property |
| Pvap | 1.79 | kPa | 263.76 | Calculated Property |
| Pvap | 14.25 | kPa | 300.83 | Calculated Property |
| Pvap | 66.08 | kPa | 337.91 | Calculated Property |
| Pvap | 214.15 | kPa | 374.99 | Calculated Property |
| Pvap | 543.00 | kPa | 412.07 | Calculated Property |
| Pvap | 1160.30 | kPa | 449.14 | Calculated Property |
| Pvap | 2197.30 | kPa | 486.22 | Calculated Property |
| Pvap | 3819.89 | kPa | 523.30 | Calculated Property |
| Pvap | [1.39e-03; 3810.53] | kPa | [189.60; 523.30] |
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 | 8.09498e+01 | |||
| Coefficient B | -6.86243e+03 | |||
| Coefficient C | -9.83731e+00 | |||
| Coefficient D | 7.27641e-06 | |||
| Coefficient E | 0.00000e+00 | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 523.30 | |||
| Pvap | 1.39e-03 | kPa | 189.60 | Calculated Property |
| Pvap | 0.10 | kPa | 226.68 | Calculated Property |
| Pvap | 1.81 | kPa | 263.76 | Calculated Property |
| Pvap | 14.29 | kPa | 300.83 | Calculated Property |
| Pvap | 66.14 | kPa | 337.91 | Calculated Property |
| Pvap | 214.41 | kPa | 374.99 | Calculated Property |
| Pvap | 544.22 | kPa | 412.07 | Calculated Property |
| Pvap | 1163.18 | kPa | 449.14 | Calculated Property |
| Pvap | 2199.72 | kPa | 486.22 | Calculated Property |
| Pvap | 3810.53 | kPa | 523.30 | Calculated Property |
| Pvap | [7.84; 97.27] | kPa | [288.73; 348.98] |
NIST
|
| Equation | ln(Y) = A + B/(T + C) Y is Pvap in kPa, T in K | |||
| Coefficient A | 1.43407e+01 | |||
| Coefficient B | -2.86833e+03 | |||
| Coefficient C | -5.51890e+01 | |||
| Reference | Polák and Mertl, 1965 | |||
| Comment | Coefficents calculated by NIST from author's data. | |||
| Temperature range, min. | 288.73 | |||
| Temperature range, max. | 348.98 | |||
| Pvap | 7.84 | kPa | 288.73 | Calculated Property |
| Pvap | 11.03 | kPa | 295.42 | Calculated Property |
| Pvap | 15.25 | kPa | 302.12 | Calculated Property |
| Pvap | 20.72 | kPa | 308.81 | Calculated Property |
| Pvap | 27.72 | kPa | 315.51 | Calculated Property |
| Pvap | 36.54 | kPa | 322.20 | Calculated Property |
| Pvap | 47.52 | kPa | 328.90 | Calculated Property |
| Pvap | 61.03 | kPa | 335.59 | Calculated Property |
| Pvap | 77.47 | kPa | 342.29 | Calculated Property |
| Pvap | 97.27 | kPa | 348.98 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| ρl | [1009.09; 311.96] | kg/m3 | [189.60; 523.25] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A / B^(1 + (1 − T/C)^D) Y is ρl in kg/m3, T in K | |||
| Coefficient A | 6.95379e+01 | |||
| Coefficient B | 2.42950e-01 | |||
| Coefficient C | 5.23260e+02 | |||
| Coefficient D | 2.57620e-01 | |||
| Comment | ChemSep eq 105, LiquidDensity | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 523.25 | |||
| ρl | 1009.09 | kg/m3 | 189.60 | Calculated Property |
| ρl | 971.80 | kg/m3 | 226.67 | Calculated Property |
| ρl | 932.45 | kg/m3 | 263.74 | Calculated Property |
| ρl | 890.55 | kg/m3 | 300.82 | Calculated Property |
| ρl | 845.35 | kg/m3 | 337.89 | Calculated Property |
| ρl | 795.73 | kg/m3 | 374.96 | Calculated Property |
| ρl | 739.69 | kg/m3 | 412.03 | Calculated Property |
| ρl | 673.21 | kg/m3 | 449.11 | Calculated Property |
| ρl | 585.36 | kg/m3 | 486.18 | Calculated Property |
| ρl | 311.96 | kg/m3 | 523.25 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| γ | [0.04; 0.00] | N/m | [189.60; 505.74] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is γ in N/m, T in K | |||
| Coefficient A | -2.53310e-02 | |||
| Coefficient B | 1.27150e+01 | |||
| Coefficient C | -2.64430e+00 | |||
| Coefficient D | -5.93700e-04 | |||
| Coefficient E | -2.76690e-06 | |||
| Comment | ChemSep eq 16, SurfaceTension | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 505.74 | |||
| γ | 0.04 | N/m | 189.60 | Calculated Property |
| γ | 0.03 | N/m | 224.73 | Calculated Property |
| γ | 0.03 | N/m | 259.85 | Calculated Property |
| γ | 0.02 | N/m | 294.98 | Calculated Property |
| γ | 0.02 | N/m | 330.11 | Calculated Property |
| γ | 0.02 | N/m | 365.23 | Calculated Property |
| γ | 0.01 | N/m | 400.36 | Calculated Property |
| γ | 0.01 | N/m | 435.49 | Calculated Property |
| γ | 0.00 | N/m | 470.61 | Calculated Property |
| γ | 0.00 | N/m | 505.74 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.00; 0.11] | W/m×K | [189.60; 990.21] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A·T^B / (1 + C/T + D/T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 2.32640e-07 | |||
| Coefficient B | 1.90200e+00 | |||
| Coefficient C | 1.02580e+02 | |||
| Coefficient D | -1.70150e+04 | |||
| Comment | ChemSep eq 102, VaporThermalConductivity | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 990.21 | |||
| λ | 0.00 | W/m×K | 189.60 | Calculated Property |
| λ | 0.01 | W/m×K | 278.56 | Calculated Property |
| λ | 0.02 | W/m×K | 367.51 | Calculated Property |
| λ | 0.02 | W/m×K | 456.47 | Calculated Property |
| λ | 0.03 | W/m×K | 545.43 | Calculated Property |
| λ | 0.04 | W/m×K | 634.38 | Calculated Property |
| λ | 0.06 | W/m×K | 723.34 | Calculated Property |
| λ | 0.07 | W/m×K | 812.30 | Calculated Property |
| λ | 0.09 | W/m×K | 901.25 | Calculated Property |
| λ | 0.11 | W/m×K | 990.21 | Calculated Property |
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| λ | [0.18; 0.13] | W/m×K | [189.60; 350.21] |
ChemSep v8.3 pure component data Compiled value
|
| Equation | Y = A + exp(B/T + C + D·T + E·T²) Y is λ in W/m×K, T in K | |||
| Coefficient A | 4.07710e-02 | |||
| Coefficient B | -1.27250e+02 | |||
| Coefficient C | -2.69950e-01 | |||
| Coefficient D | -5.57530e-03 | |||
| Coefficient E | 9.93630e-07 | |||
| Comment | ChemSep eq 16, LiquidThermalConductivity | |||
| Temperature range, min. | 189.60 | |||
| Temperature range, max. | 350.21 | |||
| λ | 0.18 | W/m×K | 189.60 | Calculated Property |
| λ | 0.18 | W/m×K | 207.45 | Calculated Property |
| λ | 0.17 | W/m×K | 225.29 | Calculated Property |
| λ | 0.16 | W/m×K | 243.14 | Calculated Property |
| λ | 0.16 | W/m×K | 260.98 | Calculated Property |
| λ | 0.15 | W/m×K | 278.83 | Calculated Property |
| λ | 0.14 | W/m×K | 296.67 | Calculated Property |
| λ | 0.14 | W/m×K | 314.52 | Calculated Property |
| λ | 0.13 | W/m×K | 332.36 | Calculated Property |
| λ | 0.13 | W/m×K | 350.21 | Calculated Property |
Similar Compounds
Find more compounds similar to Ethyl Acetate.
Mixtures
- Acetonitrile + Ethyl Acetate
- Ethanol + Acetone + Ethyl Acetate
- Ethanol + Acetone + Ethyl Acetate + Water
- Acetone + Ethyl Acetate
- Trichloromethane + Acetone + Ethyl Acetate
- n-Hexane + Acetone + Ethyl Acetate
- Acetone + Ethyl Acetate + Methyl Alcohol
- Acetone + Ethyl Acetate + Methyl Alcohol + Water
- Acetone + Ethyl Acetate + Water
- 1,2-Ethanediol + Ethanol + Ethyl Acetate
- 1,2-Ethanediol + Ethyl Acetate
- Ethanol + Ethyl Acetate
- Ethanol + 1-Butanol + Ethyl Acetate
- Ethanol + 1-Butanol + Acetic acid, butyl ester + Ethyl Acetate
- 2-Propanol + Ethanol + Ethyl Acetate
- Ethanol + Acetic acid + Ethyl Acetate + Water
- Ethanol + Acetic acid, butyl ester + Ethyl Acetate
- Ethanol + Ethyl Acetate + Methyl Alcohol
- Ethanol + Ethyl Acetate + Water
- Ethyl ether + Ethyl Acetate
Find more mixtures with Ethyl Acetate.
Sources
- KDB Vapor Pressure Data
- ChemSep v8.3 pure component data Converted from ChemSep v8.3 pure component data, H. Kooijman and R. Taylor (2021, 2022), Artistic License 2.0; see how the values differ.
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Temperature and Pressure Dependence of the Volumetric Properties of Binary Liquid Mixtures Containing Dihaloalkanes
- Experimental Determination of Densities and Isobaric Vapor Liquid Equilibria of Methyl Acetate and Ethyl Acetate with Alcohols (C3 and C4) at 0.3 MPa
- Solubility of Baicalein in Different Solvents from (287 to 323) K
- Excess Volumes and Excess Isentropic Compressibilities of Binary Liquid Mixtures of Trichloroethylene with Esters at 303.15 K
- Vapour liquid equilibrium for the ethyl ethanoate + 1-butene, +cis-2-butene, +trans-2-butene, +2-methylpropene, +n-butane and +2-methylpropane
- Revision of the volumetric method for measurements of liquid liquid equilibria in binary systems
- Activity coefficient at infinite dilution, azeotropic data, excess enthalpies and solid liquid-equilibria for binary systems of alkanes and aromatics with esters
- Vapor liquid equilibria for the quaternary reactive system ethyl acetate + ethanol +water + acetic acid and some of the constituent binary systems at 101.3 kPa
- Enhancement of liquid phase splitting of water + ethanol + ethyl acetate mixtures in the presence of a hydrophilic agent or an electrolyte substance
- (Liquid + liquid) equilibria of (water + 1-propanol + solvent) at T = 298.2K
- Vapor liquid equilibria for the ternary system of carbon dioxide + ethanol + ethyl acetate at elevated pressures
- Determination and correlation of vapor liquid equilibrium for binary systems consisting of close-boiling components
- Liquid liquid equilibria of 1,3-dimethylimidazolium methyl sulfate with ketones, dialkyl carbonates and acetates
- 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
- Vapor liquid equilibria for the binary mixtures of 2,3-butanediol with n-butanol, n-butyl acetate, and ethyl acetate at 101.3 kPa
- Determination and correlation of molar excess enthalpies of binary systems 2,4-pentanedione + (1-butanol, + 2-methyl-1-propanol, + 1-pentanol, + 1-heptane, + ethyl acetate, and + water)
- Liquid liquid equilibria of water + 2,3-butanediol + ethyl acetate at several temperatures
- Measurements of the solubilties of m-phthalic acid in acetone, ethanol and acetic ether
- Isothermal vapor liquid equilibria for different binary mixtures involved in the alcoholic distillation
- Solubility and limiting activity coefficient of simvastatin in different organic solvents
- Experimental measurements of vapor liquid equilibria at low pressure: Systems containing alcohols, esters and organic acids
- Phase equilibria for reactive distillation of diethyl succinate. Part II: Systems diethyl succinate + ethyl acetate + water and diethyl succinate + acetic acid + water
- Excess molar enthalpies of diethyl malonate+ (1-butanol, 2-methyl-1-propanol, 1-pentanol, n-heptane, and ethyl acetate) at T= (288.2, 298.2, 313.2, 328.2, 338.2, and 348.2 K) and p = 101.3 kPa
- Vapor-liquid equilibrium data for the binary systems in the process of synthesizing diethyl carbonate
- Solubilities of cinnamic acid esters in binary mixtures of ionic liquids and organic solvents
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Liquid-liquid equilibria of water + 3-hydroxy-2-butanone + ethyl ethanoate
- Determination of the solubility, dissolution enthalpy and entropy of Deflazacort in different solvents
- Experimental determination and calculation of the critical curves for the binary systems of CO2 containing ketone, alkane, ester and alcohol, respectively
- Thermodynamic analysis and enthalpy-entropy compensation for the solubility of indomethacin in aqueous and non-aqueous mixtures
- Phase equilibria in binary mixtures with monoethyl succinate
- 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
- Solubility of naproxen in ethyl acetate + ethanol mixtures at several temperatures and correlation with the Jouyban-Acree model
- New high pressure vapor-liquid equilibrium data and density predictions for carbon dioxide + ethyl acetate system
- 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
- Vapour-liquid and chemical equilibria in the ethyl ethanoate + ethanol + propyl ethanoate + propanol system accompanied with transesterification reaction
- Measurement and correlation for solubility of levofloxacin in six solvents at temperatures from 288.15 to 328.15 K
- Solubility of lansoprazole in different solvents
- Determination of the solubility, dissolution enthalpy and entropy of suberic acid in different solvents
- Experimental and calculated liquid-liquid equilibrium data for water + furfural + solvents
- A novel static analytical apparatus for phase equilibrium measurements
- 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
- Measurement and correlation solubility and mixing properties of dimethyl succinylsuccinate in pure and mixture organic solvents from (278.15 to 333.15) K
- Solubilities of crotonic acid in different organic solvents at severaltemperatures from (278.15 to 333.15) K
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
- Determination and correlation of excess molar enthalpies of thebinary carbon dioxide + ethyl acetate system at 298.15 to 308.15 K and 5.0 to 7.0 MPa
- 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
- 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
- Solubility, liquid-liquid equilibrium and critical states for the quaternary system acetic acid-ethanol-ethyl acetate-water at 303.15 K and 313.15 K
- Thermodynamics of risperidone and solubility in pure organic solvents
- Temperature dependence of limiting activity coefficients, Henry's law constants, and related infinite dilution properties of C4-C6 isomeric n-alkyl ethanoates/ethyl n-alkanoates in water. Measurement, critical compilation, correlation, and recommended data
- Phase equilibria and excess properties for binary systems in reactive distillation processes Part II. Ethyl acetate synthesis
- Solubility and tie-line data for ternary aqueous mixtures of cyclopentanol with organic solvents at T = 298.2 K: Experiments and NRTL model
- Measurement and correlation of the solubility of N-(phosphonomethyl)iminodiacetic acid in different organic solvents
- tert-Butyl chloride as a probe of the solvophobic effects
- Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
- Solubility of methylphosphonic acid in selected organic solvents
- Thermodynamic analysis for solid liquid equilibrium of mercaptosuccinic acid in a binary solvent of methanol and ethyl acetate at temperatures between (278.15 and 333.15) K
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Measurement and correlation of solubility of D-camphor-10-sulfonic acid in pure solvents
- Thermodynamic models for determination of the solubility of omeprazole sulfide in (ethanol + ethyl acetate) binary solvent mixtures
- Solution thermodynamics of simvastatin in pure solvents and binary solvent mixtures
- Solubility correlation and thermodynamic analysis of two forms of Metaxalone in different pure solvents
- Liquid-liquid equilibrium data for water + formic acid + solvent (butyl acetate, ethyl acetate, and isoamyl alcohol) at T = 291.15 K
- 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
- Solid-liquid phase equilibrium and ternary phase diagrams of ethenzamide-saccharin cocrystals in different solvents
- Liquid-liquid equilibrium data for (n-hexane + ethyl acetate + acetonitrile) ternary system at (298.15, 308.15, and 318.15) K
- A model to calculate concentration-dependent surface tension of binary systems
- The isobaric vapor liquid equilibria of ethyl acetate p acetonitrile p bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
- Separation of ethyl acetate and 2-propanol azeotropic mixture using ionic liquids as entrainers
- Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
- Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- The solubility of maleic acid in various inorganic salts and organic solvents: Thermodynamics model and parameters
- Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
- Separation of ethyl acetate and ethanol azeotrope mixture using dialkylphosphates-based ionic liquids as entrainers
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Solubility of 1,1-diamino-2,2-dinitroethylene in different pure solvents and binary mixtures (dimethyl sulfoxide p water) and (N,N-dimethylformamide p water) at different temperatures
- 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
- Liquid-liquid equilibria and COSMO-SAC modeling of organic solvent/ ionic liquid - hydroxyacetone - water mixtures
- Liquid-liquid equilibrium data for ternary systems of water + acetic acid + acetate esters at 293.2 K and 303.2 K and ~ 95 kPa
- 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
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Solubility of citalopram hydrobromide in(ethanol + toluene) and (ethanol + ethyl acetate) at 283.15-318.15 K and its correlation with the Jouyban-Acree and CNIBS/R-K models
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Solubility of cinnamic acid in supercritical carbon dioxide and subcritical 1,1,1,2-tetrafluoroethane: Experimental data and modelling
- Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
- Phase equilibrium measurements and thermodynamic modeling of {CO2 + diethyl succinate + cosolvent} systems
- Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
- Thermodynamic properties of (an ester + an alkane). XVI. Experimental HEm and V Em values and a new correlation method for (an alkyl ethanoate + an n-alkane) at 318.15 K
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) I: HE and V E for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1-x)a,x-ClCH2(CH2)v-2CH2Cl}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Thermodynamic study of (alkyl esters + a,x-alkyl dihalides) II: HE m and V E m for 25 binary mixtures {xCu-1H2u-1CO2C2H5 + (1 - x)a,x-BrCH2(CH2)v-2CH2Br}, where u = 1 to 5, a = 1 and v = x = 2 to 6
- Properties of ionic liquid HMIMPF6 with carbonates, ketones and alkyl acetates
- Molecular interactions in (2,4,6-trimethyl-1,3,5-trioxane + n-alkyl acetates) at T=(298.15, 303.15, and 308.15) K
- Determination of solvation and specific interaction enthalpies of adamantane derivatives in aprotic solvents
- Effects of the presence of ethylacetate or benzene on the densities and volumetric properties of mixture (styrene + N,N-dimethylformamide)
- Mixing properties of binary mixtures presenting azeotropes at several temperatures
- Ternary (liquid + liquid) equilibria of the azeotrope (ethyl acetate + 2-propanol) with different ionic liquids at T = 298.15 K
- Density, dynamic viscosity, and derived properties of binary mixtures of methanol or ethanol with water, ethyl acetate, and methyl acetate at T = (293.15, 298.15, and 303.15) K
- 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
- Ternary excess molar volumes of {methyltrioctylammonium bis(trifluoromethylsulfonyl)imide + ethanol + methyl acetate, or ethyl acetate} systems at T = (298.15, 303.15, and 313.15) K
- Measurement and correlation of solubilities of apigenin and apigenin 7-O-rhamnosylglucoside in seven solvents at different temperatures
- A volumetric and viscosity study for the binary mixtures of 1-hexyl-3-methylimidazolium tetrafluoroborate with some molecular solvents
- Interactions of volatile organic compounds with the ionic liquid 1-ethyl-3-methylimidazolium tetracyanoborate
- Solubilities of some organic solutes in 1-ethyl-3-methylimidazolium acetate. Chromatographic measurements and predictions from COSMO-RS
- 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
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Volumetric properties of ternary (IL + 2-propanol or 1-butanol or 2-butanol + ethyl acetate) systems and binary (IL + 2-propanol or 1-butanol or 2-butanol) and (1-butanol or 2-butanol + ethyl acetate) systems
- 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
- The potential of head-space gas chromatography for VLE measurements
- Low pressure carbon dioxide solubility in pure electrolyte solvents for lithium-ion batteries as a function of temperature. Measurement and prediction
- Volumetric properties of binary mixtures of N-ethylformamide with tetrahydrofuran, 2-butanone and ethylacetate from (293.15 to 313.15) K
- Excess molar enthalpies for mixtures of supercritical CO2 and ethyl acetate and their role in supercritical fluid applications
- Correlation and prediction of mixing thermodynamic properties of ester-containing systems: Ester + alkane and ester + ester binary systems and the ternary dodecane + ethyl pentanoate + ethyl ethanoate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium trifluorotris(perfluoroethyl)phosphate
- Measurement and correlation of the solubility of 2,3,4,5-tetrabromothiophene in different solvents
- Activity coefficient at infinite dilution measurements for organic solutes (polar and non-polar) in fatty compounds: Saturated fatty acids
- 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
- Henry s constants and activity coefficients of some organic solutes in 1-butyl,3-methylimidazolium hydrogen sulfate and in 1-methyl,3-trimethylsilylmethylimidazolium chloride
- Interactions of volatile organic compounds with the ionic liquids 1-butyl-1-methylpyrrolidinium tetracyanoborate and 1-butyl-1-methylpyrrolidinium bis(oxalato)borate
- 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
- 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
- Solubilities of p-coumaric and caffeic acid in ionic liquids and organic solvents
- Density, refraction index and vapor-liquid equilibria of N-methyl-2-hydroxyethylammonium butyrate plus (methyl acetate or ethyl acetate or propyl acetate) at several temperatures
- 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
- Infinite dilution activity coefficients of volatile organic compounds in two ionic liquids composed of the tris(pentafluoroethyl) trifluorophosphate ([FAP]) anion and a functionalized cation
- Thermodynamics of fenoxycarb in solution
- 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
- Measurement and correlation of solubility of dodecanedioic acid in different pure solvents from T = (288.15 to 323.15) K
- Measurement of activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-hexyl-1,4-diaza[2.2.2]bicyclooctanium bis(trifluoromethylsulfonyl)imide using gas-liquid chromatography
- Activity coefficients at infinite dilution of organic solutes in 1-hexyl-3- methylimidazolium trifluoroacetate and influence of interfacial adsorption using gas liquid chromatography
- Study on thermo physical and excess molar properties of binary systems of ionic liquids. I: [Cnmim][PF6] (n = 6, 8) and alkyl acetates
- 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
- Thermodynamics and activity coefficients at infinite dilution for organic solutes, water and diols in the ionic liquid choline bis(trifluoromethylsulfonyl)imide
- 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
- Determination and correlation of solubility of spironolactone form II in pure solvents and binary solvent mixtures
- (Liquid + liquid) equilibria for mixtures of dodecane and ethanol with alkylsulfate-based ionic liquids
- Thermodynamics of 4'-bromomethyl-2-cyanobiphenyl in different solvents
- Blood porphyrins in binary mixtures of N,N-dimethylformamide with 1-octanol and chloroform: The energetics of solvation, (solute + cosolvent) interactions and model calculations
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- (Solid + liquid) phase diagram for (indomethacin + nicotinamide)- methanol or methanol/ethyl acetate mixture and solubility behavior of 1:1 (indomethacin + nicotinamide) co-crystal at T = (298.15 and 313.15) K
- Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
- 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 prediction of clopidogrel hydrogen sulfate polymorphs in isopropanol and ethyl acetate
- 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
- Isothermal (vapour + liquid) equilibrium (VLE) for binary mixtures containing diethyl carbonate, phenyl acetate, diphenyl carbonate, or ethyl acetate
- Thermodynamic equilibrium of 4-hydroxy-2,5-dimethyl-3(2H)-furanone in different solvent systems
- Correlation and thermodynamic analysis of solubility of diphenhydramine hydrochloride in pure and binary solvents
- Measurement and correlation of the solubility of rivaroxaban (form I) in binary mixtures of ethyl acetate with tetrahydrofuran, N,N-dimethylformamide, and N,N-dimethylacetamide from T = (278.15 to 318.15) K
- 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
- Measurement and correlation of solubility and solution thermodynamics of 1,3-dimethylurea in different solvents from T = (288.15 to 328.15) K
- 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
- Thermodynamic models for determination of the solubility of 4-(4-aminophenyl)-3-morpholinone in different pure solvents and (1,4-dioxane + ethyl acetate) binary mixtures with temperatures from (278.15 to 333.15) K
- Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated 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
- 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 thermodynamic function of a bioactive compound bergenin in various pharmaceutically acceptable neat solvents at different temperatures
- Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
- Solubility determination and thermodynamic models for dehydroepiandrosterone acetate in mixed solvents of (ethyl acetate + methanol), (ethyl acetate + ethanol) and (ethyl acetate + isopropanol)
- 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
- 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
- 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
- Solubility of cefoxitin acid in different solvent systems
- Solid-liquid phase equilibrium and mixing properties of 2-Cyano-4'-methylbiphenyl in pure solvents
- Solubility determination and thermodynamic modelling of 2,4-dihydro-5-methyl-2-(4-methylphenyl)-3H-pyrazol-3-one in twelve organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- Thermodynamics and limiting activity coefficients measurements for organic solutes and water in the ionic liquid 1-dodecyl-3-methylimidzolium bis(trifluoromethylsulfonyl) imide
- 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
- 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
- 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 determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
- Thermodynamic modelling for solubility of 5-chloro-1-methyl-4-nitroimidazole in eleven organic solvents from T = (283.15 to 318.15) K
- Measurement and correlation of solubility of ciclesonide in seven pure organic 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
- 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 thermodynamic modelling for 2-methyl-6-nitroaniline solubility in binary solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
- Determination and correlation of terephthaldialdehyde solubility in (ethanol, isopropanol, ethyl acetate, isopentanol) + N,Ndimethylformamide mixed solvents at temperatures from 273.15 K to 318.15 K
- 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 properties of vanillyl alcohol in some pure solvents
- 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
- Liquid-liquid equilibrium for ternary systems of ethyl acetate/isopropyl acetate + 2,2,3,3-tetrafluoro-1-propanol + water at 298.15, 318.15 K
- 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 of 2-nitro-p-phenylenediamine in nine pure solvents and mixture of (methanol + N-methyl-2-pyrrolidone) from T = (283.15 to 318.15) K: Determination and modelling
- Solubility of 4-methyl-2-nitroaniline in fourteen organic solvents from T = (278.15 to 313.15) K and mixing properties of solutions
- 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
- 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 properties of enantiotropic polymorphs of glycolide
- 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
- Measurement and correlation of solubility of boscalid with thermodynamic analysis in pure and binary solvents from 288.15 K to 313.15 K
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- Thermodynamic functions for solubility of 2-mercaptobenzothiazole in eleven pure organic solvents at temperatures from 273.15 K to 318.15 K and mixing properties of solutions
- Solubility modelling, solution thermodynamics and preferential solvation for nitroxoline in solvent mixtures of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
- Solubility and preferential solvation of 2-methyl-4-nitroaniline in mixed solvents of ethyl acetate + (methanol, ethanol, n-propanol and isopropanol)
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Measurement and correlation of ternary phase equilibrium of (hexane + ethyl acetate) with four ILs
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Estimation and confirmation of the thermodynamic stability relationships of the enantiotropic polymorphs of glycolide
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Abraham model correlations for describing the thermodynamic properties of solute transfer into pentyl acetate based on headspace chromatographic and solubility measurements
- Thermodynamics and selectivity of separation based on activity coefficients at infinite dilution of various solutes in ionic liquid [HMMIM][BF4]
- The use of ionic liquids for separation of binary hydrocarbons mixtures based on gamma infinity data measurements
- Thermodynamics and activity coefficients at infinite dilution for organic compounds in the ionic liquid 1-hexyl-3-methylimidazolium chloride
- Separation of binary mixtures based on gamma infinity data using [OMMIM][BF4] ionic liquid and modelling of thermodynamic functions
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
- Solubility parameter of lenalidomide for predicting the type of solubility profile and application of thermodynamic model
- Solubility and thermodynamic properties of dirithromycin form A and form B in pure solvents and binary solvent mixture
- Equilibrium solubility of dinitolmide in several neat solvents and binary aqueous co-solvent mixtures: Experimental determination and thermodynamic analysis
- Determination and correlation of solubility and solution thermodynamics of saccharin in different pure solvents
- Determination and correlation of solubility and solution thermodynamics of musk xylene in different pure solvents
- Liquid-liquid equilibrium study for ternary systems of water + propargyl alcohol + solvents at 308.2 K: Measurement and thermodynamic modelling
- Isobaric vapor-liquid equilibrium of a ternary system of ethyl acetate + propyl acetate + dimethyl sulfoxide and binary systems of ethyl acetate + dimethyl sulfoxide and propyl acetate + dimethyl sulfoxide at 101.3 kPa
- The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
- Measurement of the thermal conductivity of five aliphatic esters in the liquid phase
- Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
- Solubility of clopidogrel hydrogen sulfate polymorphs in ethyl acetate + 2-butanol mixtures at 283.15-313.15 K
- Improving the solubility of temozolomide by cosolvent and its correlation with the Jouyban-Acree and CNIBS/R-K models
- Densities, speeds of sound, isentropic compressibilities, refractive indexes, and viscosities of tetrahydrofuran with haloalkane or alkyl ethanoate at T = 303.15 K
- Studies of viscosities of dilute solutions of alkylamine in non-electrolyte solvents. II. Haloalkanes and other polar solvents
- Molar excess enthalpies of ethyl acetate + alkanols at T=298.15K, p=10MPa
- Volumetric and transport properties of ternary mixtures containing 1-propanol + ethyl ethanoate + cyclohexane or benzene at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Volumetric and transport properties of ternary mixtures containing 1-alkanol + ethyl ethanoate + cyclohexane at 303.15 K: Experimental data, correlation and prediction by ERAS model
- Studies on liquid liquid interactions of some ternary mixtures by density, viscosity, ultrasonic speed and refractive index measurements
- Effect of electrostatic interaction on thermochemical behavior of 12-crown-4 ether in various polar solvents
- Standard enthalpies and heat capacities of ethyl acetate and deuteroporphyrin dimethylester solution in N,N-dimethylformamide at 298 318 K
- Solubilities of benzene sulfonamide in supercritical CO2 in the absence and presence of cosolvent
- 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
- Solvation of the photodynamic therapy agent in the model lipid protein system: The evidence of porphyrin preferential solvation by apolar environment
- Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
- Solution Enthalpies of 1,4-Dioxane: Study of Solvent Effects Through Quantitative Structure-Property Relationships
- Effects of temperature and concentration on interactions in (methanol + ethyl acetate) and (ethanol + methyl acetate or ethyl acetate) systems: insights from apparent molar volume and apparent molar isentropic compressibility study
- 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
- 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
- Determination and correlation of solubility and mixing properties of isonicotinamide (form II) in some pure solvents
- The study of excess molar volumes and related properties for binary mixtures containing benzyl alcohol and 1,3-dichloro-2-propanol with vinyl acetate, ethyl acetate and t-butyl acetate at T = 293.15 to 313.15 K and P = 0.087 MPa
- 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
- Experimental solubility and thermodynamic aspects of methylene blue in different solvents
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Density and Surface Tension of Binary Mixtures of 2,2,4-Trimethylpentane + n-Heptane, 2,2,4-Trimethylpentane + n-Octane, Ethyl Acetate + Benzene, and Butanenitrile + Benzene from (293.15 to 323.15) K
- Dependence of Refractive Index on Concentration and Temperature in Electrolyte Solution, Polar Solution, Nonpolar Solution, and Protein Solution
- 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
- Determination and Correlation of Solubility of N-tertbutylacrylamide in Seven Different Solvents at Temperatures between (279.15 and 353.15) K
- Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
- Solubility of Amorphous Clopidogrel Hydrogen Sulfate in Different Pure Solvents
- Lamotrigine Solubility in Some Nonaqueous Solvent Mixtures at 298.2 K
- Solubility and Thermodynamic Analysis of Tenoxicam in Different Pure Solvents at Different Temperatures
- Investigation of Surface and Solubility Properties of N-Vinylimidazolium Tetrahalogenidoferrate(III) Magnetic Ionic Liquids Using Density Functional Theory
- Isobaric Vapor - Liquid Equilibrium for Ethyl acetate + Methanol + Ionic Liquids Ternary systems at 101.3 kPa
- Solubility and Dissolution Thermodynamics for 1,3,5- Trichlorobenzene in Organic Solvents
- Solubility of Trimethoprim in Selected Pure Solvents and (Water + Ethanol/2-Propanol) Mixed-Solvent Systems
- 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
- Solubility of Benzoic Acid and Aspirin in Pure Solvents Using Focused Beam Reflective Measurement
- Thermodynamic Models for Determination of the Solubility of Boc-(R)-3-Amino-4-(2, 4, 5-trifluorophenyl)butanoic acid in Different Pure Solvents and (Tetrahydrofuran + n-Butanol) Binary Mixtures with Temperatures from 280.15 to 330.15 K
- Measurement and modeling of high pressure VLE for methyl acetate or ethyl acetate with 2-butanol. Isobaric data at 1.5 MPa
- Solubility Determination and Modeling of Sodium Mononitrobenzenesulphonate in Different Solvents at Temperatures Ranging from (283.15 to 323.15) K
- Solubility Measurement and Correlation of (+)-Biotin Intermediate Lactone in Different Organic Solvents from (287.15 to 323.75) K
- Isobaric Vapor Liquid Equilibria for Ethyl Acetate + Acetonitrile + 1-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide at 101.3 kPa
- Differential Scanning Calorimetry Data and Solubility of Rosmarinic Acid in Different Pure Solvents and in Binary Mixtures (Methyl Acetate + Water) and (Ethyl Acetate + Water) from 293.2 to 313.2 K
- Solubilities of Dihydroxylammonium 5,5'-Bistetrazole-1,1'-diolate in Various Pure Solvents at Temperatures Between 293.15 and 323.15 K
- Measurement and Thermodynamic Modeling of the Solubility of Lamotrigine, Deferiprone, Cefixime Trihydrate, and Cephalexin Monohydrate in Different Pure Solvents from 283.1 to 323.1 K
- Vapor Liquid Equilibrium for Binary Mixtures of Acetates in the Direct Esterification of Fusel Oil
- 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 2-Ethylanthraquinone in Binary Mixtures of Oligooxymethylene Dimethyl Ethers with Different Number of CH2O Groups of n = 2, 3, and 4 from 293.15 to 343.15 K
- 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
- Measurement and Correlation of Solubility on Reactive Crystallization of Methyl D-(-)-4-Hydroxy-phenylglycinate
- 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
- Solubilities of Naringin Dihydrochalcone in Pure Solvents and Mixed Solvents at Different Temperatures
- Solubility of 4-Methylsulfonylacetophenone in Nine Pure Solvents and (Ethyl Acetate + n-Hexane) Binary Solvent Mixtures from 278.15 K to 328.15 K
- 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
- Measurement and Correlation of Solubility of Loratadine in Different Pure Solvents and Binary Mixtures
- Measurement and Correlation of Solubility of Amorphous Cefmetazole Sodium in Pure Solvents and Binary Solvent Mixtures
- Measurement and Correlation of the Solubility of e-CL-20 in 12 Organic Solvents at Temperatures Ranging from 278.15 to 318.15 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 Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
- Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
- Vapor Liquid Equilibrium and Excess Enthalpy Data for Systems Containing N,N-Dimethylacetamide
- Measurements and Thermodynamic Models for the Separation of 2-Methoxyethanol and Water Azeotropic Mixtures via Different Solvents
- Vapor Liquid Equilibrium of Carbon Dioxide + Ethyl Acetate + Oleic Acid Mixtures at High Pressures
- Isobaric Vapor Liquid Equilibrium for Three Binary Systems of Acetaldehyde + Ethanol, Ethyl Acetate, 1-Butanol at 101.3 kPa
- 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
- Solubility and Thermodynamic Behavior of Syringic Acid in Eight Pure and Water + Methanol Mixed Solvents
- 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)
- 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 the Solubility of Azoxystrobin in Seven Monosolvents and Two Different Binary Mixed Solvents
- 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
- Vapor-Liquid Equilibrium Data for Binary Mixtures of Dimethyl Carbonate with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, Isopropyl Acetate, n-Butyl Acetate, and Isoamyl Acetate at 93.13 kPa
- Solubility and Mixing Thermodynamics Properties of p-Toluenesulfonamide and o-Toluenesulfonamide in Seven Monosolvents at Different Temperatures
- Solubility Modeling and Mixing Properties for Benzoin in Different Monosolvents and Solvent Mixtures at the Temperature Range from 273.15 to 313.15 K
- Measurement and Correlation of the Dissolution Equilibria of o-Iodoaniline and p-Iodoaniline in Pure Solvents
- 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
- Determination and Thermodynamic Analysis of the Solubility of Limonin in Eight Organic Solvents and Ethyl Acetate + 2-Propanol Binary Solvents from 283.2 to 323.2 K
- Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
- Solubility of p-Aminobenzoic Acid Potassium in Organic Solvents and Binary (Water + Isopropyl Alcohol) Mixture at Temperatures from (283.15 to 318.15) 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
- Isobaric Vapor-liquid Equilibrium for Three Binary Systems of Ethyl Acetate + Propyl Acetate, Ethyl Acetate + Propylene Carbonate, and Propyl Acetate + Propylene Carbonate at 101.3 kPa
- 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
- Isobaric Vapor-Liquid Equilibrium Data for Binary Systems of Anisole with Methyl Acetate, Ethyl Acetate, n-Propyl Acetate, and Isopropyl Acetate at 93.9 kPa
- Solubility of 2-Chlorophenylacetic Acid in 12 Pure Solvents from T = (273.15/283.15 to 318.15) K: Determination and Modeling
- Experimental Determination and Thermodynamic Models for Solid-Liquid Equilibrium of 4-(4-Aminophenoxy)-N-methylpyridine-2-carboxamide in Pure and Binary Solvent Mixtures for T = (278.15-328.15) K
- Solid-Liquid Phase Equilibria of the Ternary System (2-Naphthaldehyde + 4-Methylphthalic Anhydride + Ethyl Acetate) at (288.15, 298.15, and 308.15) K
- 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)
- Cosolvency and Mathematical Modeling Analysis of Chloroxine in Some Binary Solvent System
- Solubility Measurement and Modeling of 2-Amino-4,6-dichoropyrimidine in Ten Pure Solvents and (Ethyl Acetate + Ethanol) Solvent Mixtures
- Experiment and Computation of Solubility and Dissolution Properties for Enalapril Maleate and Its Intermediate in Pure Solvents
- Solubility Measurement and Correlation for epsilon-2,4,6,8,10,12-Hexanitro-2,4,6,8,10,12-hexaazaisowurtzitane in Different Alkanes/Aromatic Hydrocarbon + Ethyl Acetate Binary Solvents at Temperatures of between 283.15 and 323.15 K
- Influence of Different Solvent Properties and Composition for the Solubility of Iopromide
- Effect of Ionic Liquids on the Binary Vapor-Liquid Equilibrium of Ethyl Acetate + Methanol System at 101.3 kPa
- Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary 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 and Modeling for 4-Nitrobenzonitrile in Binary Solvent Mixtures of Ethyl Acetate Plus (Methanol, Ethanol, n-Propanol, and Isopropanol)
- Solubility Determination of Nicotinamide and Its Application for the Cocrystallization with Benzoic Acid
- 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)
- Solubility of Toltrazuril and the Effect of a Cosolvent
- Activity Coefficients at Infinite Dilution of Various Solutes in Tetrapropylammonium Bromide + 1,6-Hexanediol Deep Eutectic Solvent
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- 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
- Measurement and Correlation of Solubility and Thermodynamic Properties of Vinpocetine in Nine Pure Solvents and (Ethanol + Water) Binary Solvent
- 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
- Solubility and Data Correlation of Isoniazid in Different Pure and Binary Mixed Solvent Systems from 283.15 K to 323.15 K
- Determination and Modeling of Solid-Liquid Equilibrium for Ternary Systems of Terephthaldialdehyde + 4-Hydroxybenzaldehyde + Ethyl Acetate/Acetone
- 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
- Isobaric Vapor-Liquid Phase Equilibrium Measurements for Allyl Alcohol with Chloroform, Ethyl Acetate, and Methyl Propionate at 101.3 kPa
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Experiment and Application of the Solid-Liquid Phase Equilibrium for Ternary 2-Nitro-p-phenylenediamine + Ethyl Acetate + Isopropanol and 2-Nitro-p-phenylenediamine + 4-Nitro-o-phenylenediamine + N-Methyl-2-pyrrolidone systems
- Solubility Behavior of 2-Chloro-3- (trifluoromethyl)pyridine in (Ethyl Acetate + n-Butanol, DMF + n-Butanol, DMF + Ethanol) Solvent Mixtures
- Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
- Isobaric Vapor Liquid Equilibria for Binary Mixtures of Isoamyl Acetate + Ethyl Acetate at 50 and 100 kPa
- 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
- Volumetric and FT-IR Studies of the Binary Liquid Mixtures of Tributylamine and Alkyl Ester (C1-C5)
- Effect of Ethanol and Temperature on Partition Coefficients of Ethyl Acetate, Isoamyl Acetate, and Isoamyl Alcohol: Instrumental and Predictive Investigation
- Determination and Thermodynamic Modeling of Solid-Liquid Phase Equilibrium for Succinic Acid in the Glutaric Acid + Adipic Acid + Ethyl Acetate Mixture and Adipic Acid in the Succinic Acid + Glutaric Acid + Ethyl Acetate Mixture
- Determination and Modeling of Solubility of 4-Aminobenzamide in Different Pure Solvents
- 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
- Measurement and Correlation of the Solubility of 2-Cyanoacetamide in 14 Pure Solvents and the Mixing Properties of Solutions
- Solubilities of 2,6-Dimethylnaphthalene in Six Pure Solvents and Two Binary Solvent Systems
- Solubility Determination of 1,5-Naphthalenediamine and 1,8-Naphthalenediamine in Different Solvents and 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
- 4-Nitrophenzylcyanide Solubility in Several Nonaqueous Solvent Mixtures: Determination and Modeling
- Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
- 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
- Solubility Determination and Modeling of p-Nitrobenzamide Dissolved in Twelve Neat Solvents from 283.15 to 328.15 K
- Thermodynamic Models for Determination of Solid-Liquid Equilibrium of the Buprofezin in Pure and Binary Organic Solvents
- Solubility Determination and Thermodynamic Modeling of 2-Mercaptobenzimidazole in 12 Solvents from T = 278.15 K to T = 318.15 K
- Reactive Extraction of Gallic Acid Using Tributyl Phosphate in Different Classes of Diluents
- Measurement and Correlation of Solubility of Hydrochlorothiazide in Monosolvents and Binary Solvent Mixtures from 283.15 to 323.15 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
- Solubility of d-Tryptophan and l-Tyrosine in Several Organic Solvents: Determination and Solvent Effect
- 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
- Determination and Correlation of the Solubility of Musk Ketone in Pure and Binary Solvents at 273.15-313.15 K
- Effect of Cosolvents on the Solubility of Lenalidomide and Thermodynamic Model Correlation of Data
- 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
- 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
- Solid-Liquid Phase Equilibrium for Ternary Systems of p-Nitroacetophenone plus m-Nitroacetophenone plus Methanol/Toluene/Ethyl Acetate
- Solubility, Solubility Modeling, and Antisolvent Precipitation of 1,3-Bis(9-carbazolyl)benzene in Organic Solvents
- 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 Study and Mixing Property of 3,5-Dinitro-2-methylbenzoic Acid in 13 Pure Solvents from 288.15 to 333.15 K
- Measurement and Correlation of the Solubility of Aminocaproic Acid in Some Pure and Binary Solvents
- 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 of Acetoguanamine in Twelve Neat Solvents from 283.15 to 323.15 K
- Thermodynamic Modeling and Solubility Measurement of Cetirizine Hydrochloride and Deferiprone in Pure Solvents of Acetonitrile, Ethanol, Acetic Acid, Sulfolane, and Ethyl Acetate and Their Mixtures
- 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 of VLE Data by Using an Experimental Installation with Automatic Control: Modeling of Binary Systems of Methyl Acetate or Ethyl Acetate with n-Heptane or 2,2,4-Trimethylpentane at Both 0.1 and 1.5 MPa
- Solubility measurement and thermodynamic model correlation of sancycline in twelve pure solvents
- 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 and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
- Thermodynamic Solubility and Mixing Properties of Phenformin in 14 Pure Solvents at Temperatures Ranging from 278.15 to 323.15 K
- Solid-Liquid Phase Equilibrium and Thermodynamic Analysis of N,N'-Diethylthiourea in Different Solvent Systems
- Thermodynamic Properties of Mixtures Containing Precursors of Vitamin B5
- Isobaric Vapor-Liquid Equilibria and Excess Quantities for Binary Mixtures of an Ethyl Ester + tert-Butanol and a New Approach to VLE Data Processing
- Measurement of the Effect of Salt on Vapor-Liquid Equilibria by Using Headspace Gas Chromatography
- Total Vapor Pressure Measurements for 2-Ethoxyethanol with Methyl Acetate, Ethyl Acetate, Propyl Acetate, and Ethyl Propionate at 313.15 K and for 2-Ethoxyethanol with Methyl Formate at 308.15 K
- 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
- Density, Refractive Index, and Speed of Sound at 298.15 K and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + 1-Pentanol and Ethanol + 2-Methyl-1-propanol
- Densities, Excess Molar Volumes, Viscosities, Speeds of Sound, Excess Isentropic Compressibilities, and Relative Permittivities for Alkyl (Methyl, Ethyl, Butyl, and Isoamyl) Acetates + Glycols at Different Temperatures
- Densities and Viscosities of Binary Liquid Mixtures of Trichloroethylene and Tetrachloroethylene with Some Polar and Nonpolar Solvents
- Vapor-Liquid Equilibria of the Carbon Dioxide + Ethyl Propanoate and Carbon Dioxide + Ethyl Acetate Systems at Pressure from 2.96 MPa to 11.79 MPa and Temperature from 313 K to 393 K
- 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
- Isothermal Vapor-Liquid Equilibria of ethyl acetate + dibromomethane, or + bromochloromethane or + 1,2-dichloroethane or +1-bromo-2-chloroethane at T = 313.15 K
- Dynamic Viscosities, Densities, and Speed of Sound and Derived Properties of the Binary Systems Acetic Acid with Water, Methanol, Ethanol, Ethyl Acetate and Methyl Acetate at T = (293.15, 298.15, and 303.15) K at Atmospheric Pressure
- Solubility of 11r-Hydroxy-16r,17r-Epoxyprogesterone in Different Solvents between 283 K and 323 K
- Density, Viscosity, Refractive Index, and Speed of Sound for Binary Mixtures of 1,4-Dioxane with Different Organic Liquids at (298.15, 303.15, and 308.15) K
- Liquid-Liquid Equilibrium for the Quaternary System Toluene + Water + Propionic Acid + Ethyl Acetate at 25 deg C and Atmospheric Pressure
- Critical Properties of the Reacting Mixture in the Esterification of Acetic Acid with Ethanol
- 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
- Measurement of Activity Coefficients at Infinite Dilution of Benzene, Toluene, Ethanol, Esters, Ketones, and Ethers at Various Temperatures in Water Using the Dilutor Technique
- Solubilities of Proxetine Hydrochloride Hemihydrate between 286 K and 363 K
- Concentration Dependence of Surface Tension for Very Dilute Aqueous Solutions of Organic Non-Electrolytes
- Density and Viscosity Correlation for Several Common Fragrance and Flavor Esters
- Liquid-Liquid Equilibria for Water + Benzonitrile + Ethyl Acetate or + Butyl Acetate
- Solubility of Lovastatin in Acetone, Methanol, Ethanol, Ethyl Acetate, and Butyl Acetate between 283 K and 323 K
- Solubility, Density, and Metastable Zone Width of the (1,4-Dioxan-2-one + Ethyl Acetate) System
- Solubility of 16.alpha.,17.alpha.-Epoxyprogesterone in Six Different Solvents
- Liquid-Liquid Equilibria for the Ternary Systems Water + 3-Methyl-2-cyclopentenone with Ethyl Acetate or Methyl tert-Butyl Ether at 293.2 K
- Solubility of Hydroquinone in Different Solvents from 276.65 K to 345.10 K
- Solid-Liquid Equilibria of the trans-1,2-Cyclohexanediol + Ethyl Acetate + Water Ternary System
- 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 of Binary Mixtures Containing Ethyl Acetate + 2-Methyl-1-propanol and Ethyl Acetate + 2-Methyl-1-butanol at 101.3 kPa
- Solubilities of 2-(6-Oxido-6H-dibenz[c,e][1,2]oxaphosphorin-6-yl)-methanol in the Selected Solvents
- Volumetric Behavior and Saturated Pressure for Carbon Dioxide + Ethyl Acetate at a Temperature of 313.15 K
- Densities, Viscosities, and Refractive Indices for Binary and Ternary Mixtures of N,N-Dimethylacetamide (1) + 2-Methylbutan-2-ol (2) + Ethyl Acetate (3) at 298.15 K for the Liquid Region and at Ambient Pressure
- Activity Coefficients at Infinite Dilution in 1-Alkyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Distribution of Butyric Acid between Water and Several Solvents
- Density, Refractive Index, Speed of Sound at 298.15 K, and Vapor-Liquid Equilibria at 101.3 kPa for Binary Mixtures of Ethyl Acetate + Ethyl Lactate and Methyl Acetate + Ethyl Lactate
- Liquid-Liquid Equilibrium Diagrams of Ethanol + Water + (Ethyl Acetate or 1-Pentanol) at Several Temperatures
- Solubility and Melting Properties of Salicylic Acid
- Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
- Solubility and Melting Properties of Salicylamide
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- PVT Property Measurements for Some Aliphatic Esters from (298 to 393) K and up to 35 MPa
- Density and Speed of Sound of Binary Mixtures of N-Methylacetamide with Ethyl Acetate, Ethyl Chloroacetate, and Ethyl Cyanoacetate in the Temperature Interval (303.15 to 318.15) K
- Solubility of Acephate in Different Solvents from (292.90 to 327.60) K
- Viscosities and Interfacial Properties of I-Methyl-3-butylimidazolium Hexafluorophosphate and 1-Isobutenyl-3-methylimidazolium Tetrafluoroborate Ionic Liquids
- Solubility of 1H-1,2,4-Triazole in Ethanol, 1-Propanol, 2-Propanol, 1,2-Propanediol, Ethyl Formate, Methyl Acetate, Ethyl Acetate, and Butyl Acetate at (283 to 363) K
- Solubility of 3-Nitrophthalic Acid in Different Solvents between 278 K and 353 K
- Thermodynamic Properties of Ionic Liquids in Organic Solvents from (293.15 to 303.15) K
- Solubility of 5-(Dithiolan-3-yl)pentanoic Acid in the Mixed Solvents of Cyclohexane + Ethyl Acetate, Heptane + Ethyl Acetate, and Hexane + Ethyl Acetate
- 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 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 Genistein in Water, Methanol, Ethanol, Propan-2-ol, 1-Butanol, and Ethyl Acetate from (280 to 333) K
- Solubility of Decabromodiphenyl Ether in Different Solvents at (283.0 to 323.0) K
- Solubility of 3,5-Dinitrobenzoic Acid in Supercritical Carbon Dioxide with Cosolvent at Temperatures from (308 to 328) K and Pressures from (10.0 to 21.0) MPa
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Solubilities of 2,4-Dinitro-l-phenylalanine in Monosolvents at (273.15 to 368.15) K
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Vapor-Liquid Equilibria for Ethyl Acetate + Methanol at (0.1, 0.5, and 0.7) MPa. Measurements with a New Ebulliometer
- Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
- Liquid-Liquid Equilibrium of (Water + Pentane-2,4-dione + Ethyl Ethanoate) and (Water + Pentane-2,4-dione + Cyclohexane) at (298.15 and 313.15) K
- Measurements of the Excess Properties and Vapor-Liquid Equilibria at 101.32 kPa for Mixtures of Ethyl Ethanoate + Alkanes (from C5 to C10)
- Liquid-Liquid Equilibrium in Ternary Systems Containing Ethylene Glycol, Monofunctional Benzene Derivative, and Ethyl Acetate
- Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
- Activity Coefficients at Infinite Dilution in Methylimidazolium Nitrate Ionic Liquids
- Measurement and Correlation for the Solubilities of Dihydrocapsaicin in n-Heptane, n-Hexane, n-Pentane, Ethyl Acetate, Acetone, Ethanol, and Water
- Solubility of 2-Chloro-4,6-dinitroresorcinol in Ethanol, Methanol, Acetic Acid, Ethyl Acetate, and Water
- Solubility of Dexibuprofen in Different Solvents from (263.15 to 293.15) K
- Solubilities of Phloretin in 12 Solvents at Different Temperatures
- Measurement and Correlation of the Solubility of Prednisone Acetate in Different Solvents
- Solubility of Imperatorin in Ethyl Acetate, Ethanol, Methanol, n-Hexane, and Petroleum Ether from (278.2 to 318.2) K
- Solubilities of Ursolic Acid and Oleanolic Acid in Four Solvents from (283.2 to 329.7) K
- Measurement and Correlation for Solubilities of 16-Dehydropregnenolone Acetate in Different Solvents
- 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
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Solubilities of Betulinic Acid in Thirteen Organic Solvents at Different Temperatures
- Evaluation of Excess Molar Enthalpies for a Quaternary Mixture System of Acetic Anhydride, Ethanol, Acetic Acid, and Ethyl Acetate
- Activity Coefficients at Infinite Dilution by GLC in Alkanediamines as Stationary Phases
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Determination and Correlation of Vapor Liquid Equilibrium Data for the Ethyl Acetate + Hexamethyl Disiloxane System at 101.3 kPa
- Vapor Liquid Equilibrium and Liquid Liquid Equilibrium of Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Acetate
- Solid Liquid Phase Equilibrium and Solubility of Dibenzo[b,d]furan and 9H-Fluoren-9-one in Organic Solvents
- Activity Coefficients at Infinite Dilution of Volatile Compounds in Water: Effect of Temperature and Salt Concentration
- Solubility of o-Nitrobenzoic Acid in Modified Supercritical Carbon Dioxide at (308 to 328) K
- 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)
- Solubilities of Bis(2,4,6-trimethylbenzoyl)phenylphosphine Oxide in Different Organic Solvents at Several Temperatures
- Solubility of Vitamin D3 in Six Organic Solvents at Temperatures from (248.2 to 273.2) K
- Determination and Correlation of Pyridazin-3-amine Solubility in Eight Organic Solvents at Temperatures Ranging from (288.05 to 333.35) K
- Measurement and Correlation of the Solubility of Febuxostat in Four Organic Solvents at Various Temperatures
- Densities and Speeds of Sound of Binary Liquid Mixtures of Some n-Alkoxypropanols with Methyl Acetate, Ethyl Acetate, and n-Butyl Acetate at T = (288.15, 293.15, 298.15, 303.15, and 308.15) K
- Effect of Inorganic Salts on the Isobaric Vapor Liquid Equilibrium of the Ethyl Acetate Ethanol System
- Determination and Correlation of Solubility Data and Dissolution Thermodynamic Data of l-Lactide in Different Pure Solvents
- Isobaric Vapor - Liquid Equilibrium for Ethyl Acetate + Acetonitrile + 1 - Butyl-3-methylimidazolium Hexa fl uorophosphate at 101.3 kPa
- Investigation of the Solubility of Octahydro-1,3,5,7-tetranitro-1,3,5,7-tetrazocine and 1,3,5-Triacetyl-hexahydro-s-triazine
- Solubilities of 4,4'-Dichlorodiphenyl Disulfide in Six Organic Solvents between (303.15 and 333.15) K
- Solid Liquid Equilibrium and Phase Diagram for the Ternary 4-Chlorophthalic Anhydride + 3-Chlorophthalic Anhydride + Ethyl Acetate System
- Solubility of Veratric Acid in Eight Monosolvents and Ethanol + 1-Butanol at Various Temperatures
- Vapor Liquid Equilibrium at 350 K, Excess Molar Enthalpies at 298 K, and Excess Molar Volumes at 298 K of Binary Mixtures Containing Ethyl Acetate, Butyl Acetate, and 2-Butanol
- Solubilities of 4-Amino-4?-nitrodiphenyl Sulfide in Six Organic Solvents from 287.45 K to 365.55 K
- 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 1,3,2-Dioxaphosphorinane-2-methanol-a,a-5,5-tetramethyl 2-oxide in Selected Solvents at 273.15 K to 343.15 K
- Solubility of Benzyl Disulfide in Five Organic Solvents between (283.45 and 333.15) K
- Solubilities of Phosphonic Acid, P,P'-(1,4-Piperazinediyl)bis-,P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Solubility of 3,4-Bis(3-nitrofurazan-4-yl)furoxan in Common Solvents at Temperatures between 293.15 K and 313.15 K
- Experimental Determination of Vapor Liquid Equilibria. Binary Systems of Methyl Acetate, Ethyl Acetate, and Propyl Acetate with 1-Propanol at 0.6 MPa
- Measurement and Correlation of Solubility of 2-Chloro-4-ethylamino-6-isopropylamino-1,3,5-triazine in Different Organic Solvents
- Solubility and Dissolution Thermodynamic Data of Mefenamic Acid Crystals in Different Classes of Organic Solvents
- Measurement and Correlation of Solubilities of Indole-2-carboxylic Acid in Ten Different Pure Solvents from (278.15 to 360.15) K
- Vapor Liquid Equilibrium for Several Compounds Relevant to the Biofuels Industry Modeled with the Wilson Equation
- 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
- Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
- Solubility of Dichloronitrobenzene in Eight Organic Solvents from T = (278.15 to 303.15) K: Measurement and Thermodynamic Modeling
- 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
- 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
- Liquid Liquid Equilibria for the Ternary Systems of FC3283 + HFE7300 + Hexane, FC3283 + HFE7500 + Octane, and FC72 + HFE7100 + (Acetonitrile or Ethyl Acetate) at 273.15 K, 298.15 K, and 313.15 K
- Investigation of Surface Properties and Solubility of 1-Vinyl-3-alkyl/Esterimidazolium Halide Ionic Liquids by Density Functional Methods
- Measurement and Correlation of the Solubility of Enrofloxacin in Different Solvents from (303.15 to 321.05) K
- Development of a Predictive Equation of State for CO2 + Ethyl Ester Mixtures Based on Critical Points Measurements
- 4-Amino-3,6-dichloropyridazine Solubility Measurement and Correlation in Seven Pure Organic Solvents from (278.15 to 333.15) K
- Experimental VLE data of Methyl Acetate or Ethyl Acetate with 2-Butanol at 0.3 and 0.6 MPa. Quality assessment and predictions.
- Solubility of (2Z)-N-Cyclohexyl-2-(3-hydroxybenzylidine) Hydrazine Carbothioamide in Different Pure Solvents at (298.15 to 338.15) K
- Solubility of Tetranitrodimerglycoluril (TNDGU) in Different Solvents at Temperatures between 293.15 K and 313.15 K
- Solubility and Thermodynamic Functions of Isatin in Pure Solvents
- Experimental Measurement and Correlation of Solubility Data and Thermodynamic Properties of Protocatechuic Acid in Four Organic Solvents
- Liquid Liquid Equilibrium in Mixtures Containing Propane-1,2,3-triol and Mixtures Containing Vegetable Oils at Atmospheric Pressure
- 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
- Correlation of Solubility of Bioactive Compound Reserpine in Eight Green Solvents at (298.15 to 338.15) K
- Thermal Stability and Vapor Liquid Equilibrium for Imidazolium Ionic Liquids as Alternative Reaction Media
- Experimental and Modeling Studies on the Solubility of d-Pantolactone in Four Pure Solvents and Ethanol Water Mixtures
- Solubilities of Naringin and Naringenin in Different Solvents and Dissociation Constants of Naringenin
- Determination and Correlation of Solubilities of 2-Isopropylthioxanthone (ITX) in Seven Different Solvents from (299.15 to 329.85) K
- Measurement, Correlation, and Thermodynamics of Solubility of Isatin in Nine Different Green Solvents at (298.15 to 338.15) K
- Determination and Modeling of the Solubility of 2,4-Dimethoxybenzoic Acid in Six Pure and Isopropanol + Ethyl Acetate Mixed Organic Solvents at Temperatures From (288.15 to 323.15) 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 of Atractylenolide III in Hexane, Ethyl Acetate, Diethyl Ether, and Ethanol from (283.2 to 323.2) K
- Viscosity and Density of Water + Ethyl Acetate + Ethanol Mixtures at 298.15 and 318.15 K and Atmospheric Pressure
- Solubility of a-Sitosteryl Maleate and Stigmasteryl Maleate in Acetone and Ethyl Acetate
- Solubilities of Betulin in Fourteen Organic Solvents at Different Temperatures
- High-Pressure Vapor-Liquid Equilibrium Data for Systems Involving Carbon Dioxide + Organic Solvent + a-Carotene
- Solubility of Chlorpheniramine Maleate in Ethanol, 1-Propanol, 1-Butanol, Benzene, Ethyl Acetate, Ethyl Formate, and Butyl Acetate between 283 K and 333 K
- Solubility of Triethylenediamine in Methanol, Ethanol, Isopropanol, I-Butanol, and Ethyl Acetate between 276.15 K and 363.15 K
- Solubility of 1-H-Tetrazole-1-acetic Acid in Different Solvents between 283 K and 323 K
- Solubility of Phenacetinum in Methanol, Ethanol, 1-Propanol, 1-Butanol, 1-Pentanol, Tetrahydrofuran, Ethyl Acetate, and Benzene between 282.65 K and 333.70 K
- Liquid-Liquid Equilibria of Water + 2-Butanol + (Methyl Methacrylate or Butyl Methacrylate or Isobutyl Methacrylate) at (288.2 and 318.2) K
- Solubilities of the Gaseous and Liquid Solutes and Their Thermodynamics of Solubilization in the Novel Room-Temperature Ionic Liquids at Infinite Dilution by Gas Chromatography
- Isobaric Vapor-Liquid Equilibria for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Trifluoromethanesulfonate at 100 kPa
- Ternary Liquid-Liquid Equilibria for Six Systems Containing Ethylacetate + Ethanol or Acetic Acid + an Imidazolium-Based Ionic Liquid with a Hydrogen Sulfate Anion at 313.2 K
- Solubility of Salicylic Acid in Water, Ethanol, Carbon Tetrachloride, Ethyl Acetate, and Xylene
- Separation of Ethyl Acetate and Ethanol by Room Temperature Ionic Liquids with the Tetrafluoroborate Anion
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Solubility of Gallic Acid in Methanol, Ethanol, Water, and Ethyl Acetate
- 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
- Solubilities of Adefovir Dipivoxil in Different Binary Solvents at 298.15 K
- Solubility of Losartan Potassium in Different Pure Solvents from (293.15 to 343.15) K
- 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
- Phase Equilibria of the Azeotropic Mixture Hexane + Ethyl Acetate with Ionic Liquids at 298.15 K
- 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
- Isobaric Vapor-Liquid Equilibrium for Ethyl Acetate + Ethanol + 1-Ethyl-3-methylimidazolium Tetrafluoroborate
- Determination and Correlation of Excess Molar Enthalpies of Eight Binary Systems Containing Acetophenone at Different Temperatures
- 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
- Solubility of Diamantane, Trimantane, Tetramantane, and Their Derivatives in Organic Solvents
- Solubility of Naphthalene in Isobutyl Acetate, n-Butyric Acid, Ethyl Acetate, N-Methyl Pyrrolidone, N,N-Dimethylformamide, and Tetrahydrofuran
- Solubilities of Salicylic Acid in Pure Solvents and Binary Mixtures Containing Cosolvent
- Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
- Solubility of Desmosterol in Five Organic Solvents
- Densities, Viscosities, and Speeds of Sound of Binary Liquid Mixtures of Sulfolane with Ethyl Acetate, n-Propyl Acetate, and n-Butyl Acetate at Temperature of (303.15, 308.15, and 313.15) K
- Solubility of Podophyllotoxin in Six Organic Solvents from (283.2 to 323.2) K
- Densities and Viscosities of Ternary Mixtures of Cyclohexane + Cyclohexanone + Some Alkyl Acetates at 298.15 K
- Solubility of Cloxacillin Sodium in Different Binary Solvents
- 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 of Tiamulin Hydrogen Fumarate in Acetone, Acetonitrile, Ethyl Acetate, Ethyl Formate, and Butyl Acetate from (288.2 to 318.2) K
- Solubilities of Triphenylphosphine Oxide in Selected Solvents
- 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
- Excess Molar Enthalpies of Five Binary Systems Containing Ethyl Acetoacetate at Different Temperatures
- Physical Properties of Binary and Ternary Mixtures of Ethyl Acetate, Ethanol, and 1-Octyl-3-methyl-imidazolium Bis(trifluoromethylsulfonyl)imide at 298.15 K
- Solubility of Valsartan in Ethyl Acetate + Hexane Binary Mixtures from (278.15 to 313.15) K
- Solubility of Baicalin in Methanol, Ethanol, and Ethyl Acetate from (298.2 to 328.2) K
- 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
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Solubility of Penicillin Sulfoxide in Different Solvents
- 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 Cinnamic Acid Esters in Organic Solvents
- Volumetric and Transport Properties of Binary Liquid Mixtures of Phenylacetonitrile with Aliphatic Esters at Temperatures of (303.15 to 313.15) 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
- 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
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Solubility of Anthracene in Binary and Ternary Mixtures of Cyclohexanone, Ethyl Acetate, and Methanol at 298.2 K
- Ternary Excess Molar Volumes of {Methyltrioctylammonium Bis[(trifluoromethyl)sulfonyl]imide + Methanol + Methyl Acetate or Ethyl Acetate} Systems at (298.15, 303.15, and 313.15) K
- Surface Tension Data of Aqueous Binary Mixtures of Methyl, Ethyl, Propyl, and Butyl Acetates at 298.15 K
- ss-Sitosterol Solubility in Selected Organic Solvents
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- NCMS SOLV-DB
- The Yaws Handbook of Vapor Pressure
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