- 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
- Ethyl ethanoate
- Ethylacetaat
- Ethyle (acetate d')
- Ethylester kyseliny octove
- Etile (acetato di)
- NSC 70930
- Rcra waste number U112
- UN 1173
- Vinegar naphtha
- ac. acetic ethyl ester
- 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).
- 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.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρc : Critical density (kg/m3).
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- ΔfusS : Entropy of fusion at a given temperature (J/mol×K).
- S°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 : Liquid thermal conductivity (W/m×K).
- Tfus : Normal melting (fusion) point (K).
- Ttriple : Triple Point Temperature (K).
- Vc : Critical Volume (m3/kmol).
- Zc : Critical Compressibility.
- Zra : Rackett Parameter.
- 1: Molecular weight from the IUPAC atomic weights tables.
Cheméo is a service of Céondo GmbH, since 2007, we provide simulation, modelling and software development services for the industry.
Do not hesitate to contact us for your projects.
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3620 | KDB | |
| PAff | 835.70 | kJ/mol | NIST |
| Tig | 699.82 | K | KDB |
| 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 | 1.90 | debye | KDB |
| η | [0.0004260; 0.0004370] | Pa×s |
|
| η | 0.0004370 | Pa×s | A volum... |
| η | 0.0004274 | Pa×s | Densiti... |
| η | 0.0004260 | Pa×s | Densiti... |
| LFL | 2.20 | % in Air | KDB |
| UFL | 9.00 | % in Air | KDB |
| Tflash,cc | 285.93 | K | KDB |
| Tflash,oc | 268.71 | K | KDB |
| ΔfG° | -327.60 | kJ/mol | KDB |
| Rg | 3.3480 | KDB | |
| ΔfH°gas | [-446.90; -443.20] | kJ/mol |
|
| 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° | 8.90 | kJ/mol | Joback Calculated Property |
| ΔvapH° | 33.65 | kJ/mol | Joback Calculated Property |
| 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. Sol... | |
| log10WS | -0.04 | Estimat... | |
| logPoct/wat | 0.569 | Crippen Calculated Property | |
| McVol | 74.660 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| Pc | [3830.00; 4280.00] | kPa |
|
| Pc | 3882.00 | kPa | KDB |
| Pc | 3900.00 | kPa | Critica... |
| 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 |
| 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 | 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 | 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 | 611.00 | NIST | |
| Inp | 600.00 | 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 | 600.00 | 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 | 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 | 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 | 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 | 605.00 | NIST | |
| Inp | 587.00 | NIST | |
| Inp | 595.00 | NIST | |
| Inp | 578.00 | NIST | |
| Inp | 614.00 | NIST | |
| Inp | 601.00 | NIST | |
| Inp | Outlier 633.00 | NIST | |
| Inp | 616.00 | NIST | |
| Inp | 598.00 | NIST | |
| Inp | 603.00 | NIST | |
| Inp | 596.00 | NIST | |
| Inp | 589.00 | 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 | 350.26 | K | KDB |
| Tboil | 350.27 | K | Vapor l... |
| Tboil | 350.24 | K | Vapor l... |
| Tboil | 350.24 | K | Liquid-... |
| Tboil | 350.20 | K | Solubil... |
| Tboil | 350.15 | K | The iso... |
| Tboil | 350.29 | K | Isobari... |
| Tboil | 350.35 | K | Isobari... |
| Tboil | 350.16 | K | Vapor L... |
| Tboil | 350.20 | K | Isobari... |
| Tboil | 349.95 | K | Effect ... |
| Tboil | 350.28 | K | Isobari... |
| Tboil | 350.25 | K | Isobari... |
| Tboil | 350.15 | K | Vapor-L... |
| Tboil | 350.21 | K | Volumet... |
| Tboil | 350.15 | K | Measure... |
| Tboil | 350.19 | K | Experim... |
| 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 | 523.30 | K | KDB |
| Tc | 523.29 | K | Develop... |
| 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 | [189.25; 189.50] | K |
|
| Tfus | 189.25 | K | Aq. Sol... |
| Tfus | 189.50 | K | KDB |
| Ttriple | [189.30; 189.30] | K |
|
| Ttriple | 189.30 ± 0.05 | K | NIST |
| Ttriple | 189.30 ± 0.20 | K | NIST |
| Vc | 0.286 | m3/kmol | KDB |
| Zc | 0.2551730 | KDB | |
| Zra | 0.25 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [125.82; 149.47] | J/mol×K | [360.00; 450.00] |
|
| Cp,gas | 125.82 | J/mol×K | 360.00 | NIST |
| Cp,gas | 131.06 | J/mol×K | 380.00 | NIST |
| Cp,gas | 136.22 | J/mol×K | 400.00 | NIST |
| Cp,gas | 142.80 | J/mol×K | 425.00 | NIST |
| Cp,gas | 149.47 | J/mol×K | 450.00 | NIST |
| Cp,liquid | [157.70; 170.59] | J/mol×K | [290.00; 303.61] |
|
| Cp,liquid | 157.70 | J/mol×K | 290.00 | NIST |
| Cp,liquid | 169.20 | J/mol×K | 293.60 | NIST |
| Cp,liquid | 169.50 | J/mol×K | 298.10 | NIST |
| Cp,liquid | 168.94 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 169.30 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 169.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 167.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 169.06 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 169.60 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 170.59 | J/mol×K | 298.32 | NIST |
| Cp,liquid | 168.82 | J/mol×K | 303.61 | NIST |
| η | [0.0002750; 0.0004520] | Pa×s | [293.15; 343.15] |
|
| η | 0.0004520 | Pa×s | 293.15 | Density... |
| η | 0.0004430 | Pa×s | 293.15 | Density... |
| η | 0.0004520 | Pa×s | 293.15 | Dynamic... |
| η | 0.0004260 | Pa×s | 298.15 | Density... |
| η | 0.0004280 | Pa×s | 298.15 | Densiti... |
| η | 0.0004260 | Pa×s | 298.15 | Dynamic... |
| η | 0.0004210 | Pa×s | 298.15 | Density... |
| η | 0.0003790 | Pa×s | 303.15 | Volumet... |
| η | 0.0004030 | Pa×s | 303.15 | Dynamic... |
| η | 0.0004030 | Pa×s | 303.15 | Density... |
| η | 0.0003990 | Pa×s | 303.15 | Density... |
| η | 0.0003806 | Pa×s | 303.15 | Densiti... |
| η | 0.0003810 | Pa×s | 308.15 | Density... |
| η | 0.0003610 | Pa×s | 308.15 | Volumet... |
| η | 0.0003870 | Pa×s | 308.15 | Densiti... |
| η | 0.0003622 | Pa×s | 308.15 | Densiti... |
| η | 0.0003426 | Pa×s | 313.15 | Densiti... |
| η | 0.0003630 | Pa×s | 313.15 | Density... |
| η | 0.0003440 | Pa×s | 313.15 | Volumet... |
| η | 0.0003460 | Pa×s | 318.15 | Density... |
| η | 0.0003300 | Pa×s | 323.15 | Density... |
| η | 0.0003150 | Pa×s | 328.15 | Density... |
| η | 0.0003010 | Pa×s | 333.15 | Density... |
| η | 0.0002880 | Pa×s | 338.15 | Density... |
| η | 0.0002750 | Pa×s | 343.15 | Density... |
| ΔfusH | [10.48; 10.48] | kJ/mol | [189.30; 189.30] |
|
| ΔfusH | 10.48 | kJ/mol | 189.30 | NIST |
| ΔfusH | 10.48 | kJ/mol | 189.30 | NIST |
| ΔfusH | 10.48 | kJ/mol | 189.30 | NIST |
| ΔvapH | [31.00; 36.70] | kJ/mol | [313.00; 363.00] |
|
| ΔvapH | 34.60 ± 0.10 | kJ/mol | 313.00 | NIST |
| ΔvapH | 35.70 | kJ/mol | 319.50 | NIST |
| ΔvapH | 34.00 | kJ/mol | 320.00 | NIST |
| ΔvapH | 36.70 | kJ/mol | 322.00 | NIST |
| ΔvapH | 33.80 ± 0.10 | kJ/mol | 326.00 | NIST |
| ΔvapH | 33.40 ± 0.10 | kJ/mol | 331.00 | NIST |
| ΔvapH | 31.40 ± 0.10 | kJ/mol | 343.00 | NIST |
| ΔvapH | 32.40 ± 0.10 | kJ/mol | 344.00 | NIST |
| ΔvapH | 34.10 | kJ/mol | 345.00 | NIST |
| ΔvapH | 32.22 | kJ/mol | 349.80 | KDB |
| ΔvapH | 31.90 | kJ/mol | 350.00 | NIST |
| ΔvapH | 31.94 | kJ/mol | 350.30 | NIST |
| ΔvapH | 31.90 ± 0.10 | kJ/mol | 351.00 | NIST |
| ΔvapH | 31.00 ± 0.10 | kJ/mol | 363.00 | NIST |
| Pvap | [11.89; 1500.00] | kPa | [297.17; 462.75] |
|
| Pvap | 11.89 | kPa | 297.17 | Measure... |
| Pvap | 16.04 | kPa | 303.35 | Measure... |
| Pvap | 18.33 | kPa | 306.25 | Measure... |
| Pvap | 20.64 | kPa | 308.86 | Measure... |
| Pvap | 21.72 | kPa | 310.00 | Isobari... |
| Pvap | 22.44 | kPa | 310.67 | Measure... |
| Pvap | 24.34 | kPa | 312.53 | Measure... |
| Pvap | 24.78 | kPa | 313.00 | Isobari... |
| Pvap | 25.08 | kPa | 313.15 | Total V... |
| Pvap | 25.30 | kPa | 313.15 | Isother... |
| Pvap | 27.63 | kPa | 315.44 | Measure... |
| Pvap | 28.18 | kPa | 316.00 | Isobari... |
| Pvap | 31.37 | kPa | 318.40 | Vapour ... |
| Pvap | 31.33 | kPa | 318.46 | Measure... |
| Pvap | 31.95 | kPa | 319.00 | Isobari... |
| Pvap | 34.85 | kPa | 321.01 | Measure... |
| Pvap | 36.12 | kPa | 322.00 | Isobari... |
| Pvap | 38.43 | kPa | 323.47 | Measure... |
| Pvap | 40.00 | kPa | 324.44 | Determi... |
| Pvap | 40.61 | kPa | 324.80 | Measure... |
| Pvap | 40.73 | kPa | 325.00 | Isobari... |
| Pvap | 44.98 | kPa | 327.41 | Measure... |
| Pvap | 45.80 | kPa | 328.00 | Isobari... |
| Pvap | 45.95 | kPa | 328.15 | Isother... |
| Pvap | 49.27 | kPa | 329.77 | Measure... |
| Pvap | 50.00 | kPa | 330.01 | Isobari... |
| Pvap | 51.36 | kPa | 331.00 | Isobari... |
| Pvap | 52.56 | kPa | 331.51 | Measure... |
| Pvap | 53.33 | kPa | 331.90 | Determi... |
| Pvap | 55.72 | kPa | 333.07 | Measure... |
| Pvap | 57.46 | kPa | 334.00 | Isobari... |
| Pvap | 59.91 | kPa | 335.02 | Measure... |
| Pvap | 62.83 | kPa | 336.33 | Measure... |
| Pvap | 64.13 | kPa | 337.00 | Isobari... |
| Pvap | 66.49 | kPa | 337.91 | Measure... |
| Pvap | 66.66 | kPa | 337.99 | Determi... |
| Pvap | 69.34 | kPa | 339.09 | Measure... |
| Pvap | 71.40 | kPa | 340.00 | Isobari... |
| Pvap | 72.26 | kPa | 340.23 | Measure... |
| Pvap | 76.02 | kPa | 341.69 | Measure... |
| Pvap | 79.32 | kPa | 343.00 | Isobari... |
| Pvap | 79.83 | kPa | 343.03 | Measure... |
| Pvap | 79.99 | kPa | 343.18 | Determi... |
| Pvap | 82.56 | kPa | 344.11 | Measure... |
| Pvap | 86.85 | kPa | 345.53 | Measure... |
| Pvap | 87.93 | kPa | 346.00 | Isobari... |
| Pvap | 90.81 | kPa | 346.86 | Measure... |
| Pvap | 93.32 | kPa | 347.70 | Determi... |
| Pvap | 94.63 | kPa | 348.09 | Measure... |
| Pvap | 96.74 | kPa | 348.75 | Measure... |
| Pvap | 97.26 | kPa | 349.00 | Isobari... |
| Pvap | 98.97 | kPa | 349.45 | Measure... |
| Pvap | 100.00 | kPa | 349.53 | Isobari... |
| Pvap | 99.36 | kPa | 349.56 | Measure... |
| Pvap | 100.07 | kPa | 349.76 | Measure... |
| Pvap | 100.68 | kPa | 349.93 | Measure... |
| Pvap | 101.30 | kPa | 349.95 | Effect ... |
| Pvap | 101.30 | kPa | 350.15 | The iso... |
| Pvap | 101.32 | kPa | 350.15 | Measure... |
| Pvap | 101.30 | kPa | 350.28 | Isobari... |
| Pvap | 101.30 | kPa | 350.29 | Isobari... |
| Pvap | 101.30 | kPa | 350.35 | Isobari... |
| Pvap | 104.65 | kPa | 351.12 | Measure... |
| Pvap | 106.84 | kPa | 351.77 | Measure... |
| Pvap | 107.36 | kPa | 352.00 | Isobari... |
| Pvap | 108.13 | kPa | 352.12 | Measure... |
| Pvap | 111.21 | kPa | 352.94 | Measure... |
| Pvap | 111.76 | kPa | 353.15 | Vapor L... |
| Pvap | 114.65 | kPa | 353.91 | Measure... |
| Pvap | 116.46 | kPa | 354.43 | Measure... |
| Pvap | 118.56 | kPa | 354.93 | Measure... |
| Pvap | 118.27 | kPa | 355.00 | Isobari... |
| Pvap | 120.68 | kPa | 355.50 | Measure... |
| Pvap | 122.31 | kPa | 355.91 | Measure... |
| Pvap | 124.00 | kPa | 356.37 | Measure... |
| Pvap | 127.89 | kPa | 357.35 | Measure... |
| Pvap | 130.00 | kPa | 357.92 | Measure... |
| Pvap | 130.03 | kPa | 358.00 | Isobari... |
| Pvap | 133.45 | kPa | 358.74 | Measure... |
| Pvap | 134.15 | kPa | 359.00 | Isobari... |
| Pvap | 136.34 | kPa | 359.44 | Measure... |
| Pvap | 139.07 | kPa | 360.03 | Measure... |
| Pvap | 142.55 | kPa | 360.88 | Measure... |
| Pvap | 146.37 | kPa | 361.73 | Measure... |
| Pvap | 150.43 | kPa | 362.62 | Measure... |
| Pvap | 155.58 | kPa | 363.72 | Measure... |
| Pvap | 157.94 | kPa | 364.25 | Measure... |
| Pvap | 160.53 | kPa | 364.81 | Measure... |
| Pvap | 163.99 | kPa | 365.52 | Measure... |
| Pvap | 167.81 | kPa | 366.29 | Measure... |
| Pvap | 171.33 | kPa | 367.00 | Measure... |
| Pvap | 174.65 | kPa | 367.64 | Measure... |
| Pvap | 176.37 | kPa | 367.98 | Measure... |
| Pvap | 180.88 | kPa | 368.83 | Measure... |
| Pvap | 184.43 | kPa | 369.49 | Measure... |
| Pvap | 187.47 | kPa | 370.07 | Measure... |
| Pvap | 190.92 | kPa | 370.69 | Measure... |
| Pvap | 195.35 | kPa | 371.50 | Measure... |
| Pvap | 205.70 | kPa | 373.00 | Isother... |
| Pvap | 202.90 | kPa | 373.15 | Vapor L... |
| Pvap | 557.10 | kPa | 412.80 | Isother... |
| Pvap | 687.53 | kPa | 423.15 | Vapor L... |
| Pvap | 1222.70 | kPa | 452.30 | Isother... |
| Pvap | 1500.00 | kPa | 462.75 | Measure... |
| n0 | [1.35368; 1.37519] | [288.15; 328.15] |
|
|
| n0 | 1.37519 | 288.15 | Density... | |
| n0 | 1.37490 | 288.20 | Experim... | |
| n0 | 1.35880 | 293.15 | Solubil... | |
| n0 | 1.37190 | 293.15 | Solubil... | |
| n0 | 1.37240 | 293.15 | A novel... | |
| n0 | 1.37241 | 293.15 | Mixing ... | |
| n0 | 1.37010 | 293.15 | Liquid-... | |
| n0 | 1.35880 | 293.15 | Solubil... | |
| n0 | 1.37241 | 293.15 | Thermod... | |
| n0 | 1.37190 | 293.15 | Solubil... | |
| n0 | 1.37020 | 293.20 | Vapor l... | |
| n0 | 1.37270 | 298.15 | Effects... | |
| n0 | 1.36983 | 298.15 | Physica... | |
| n0 | 1.36977 | 298.15 | Ternary... | |
| n0 | 1.37000 | 298.15 | Molecul... | |
| n0 | 1.36977 | 298.15 | Propert... | |
| n0 | 1.37120 | 298.15 | Determi... | |
| n0 | 1.37130 | 298.15 | Density... | |
| n0 | 1.36980 | 298.15 | Vapor-L... | |
| n0 | 1.37244 | 298.15 | Isobari... | |
| n0 | 1.36981 | 298.15 | Measure... | |
| n0 | 1.36980 | 298.15 | Density... | |
| n0 | 1.36977 | 298.15 | Mixing ... | |
| n0 | 1.36920 | 298.15 | Thermod... | |
| n0 | 1.36994 | 298.15 | Density... | |
| n0 | 1.36990 | 298.15 | Densiti... | |
| n0 | 1.36978 | 298.15 | Density... | |
| n0 | 1.36977 | 298.15 | Thermod... | |
| n0 | 1.37000 | 298.15 | Correla... | |
| n0 | 1.36978 | 298.15 | Liquid-... | |
| n0 | 1.37000 | 298.15 | Vapor-L... | |
| n0 | 1.36750 | 303.15 | Liquid-... | |
| n0 | 1.36712 | 303.15 | Thermod... | |
| n0 | 1.36720 | 303.15 | Density... | |
| n0 | 1.36730 | 303.15 | Density... | |
| n0 | 1.36712 | 303.15 | Mixing ... | |
| n0 | 1.36640 | 303.15 | Densiti... | |
| n0 | 1.36720 | 303.20 | Experim... | |
| n0 | 1.36460 | 308.15 | Density... | |
| n0 | 1.36310 | 308.15 | Density... | |
| n0 | 1.35919 | 318.15 | Density... | |
| n0 | 1.35970 | 318.15 | Thermod... | |
| n0 | 1.35940 | 318.20 | Experim... | |
| n0 | 1.35368 | 328.15 | Density... | |
| ρl | [830.62; 906.55] | kg/m3 | [288.15; 348.15] |
|
| ρl | 906.55 | kg/m3 | 288.15 | Excess ... |
| ρl | 901.00 | kg/m3 | 293.00 | KDB |
| ρl | 900.44 | kg/m3 | 293.15 | Density... |
| ρl | 900.57 | kg/m3 | 293.15 | Study o... |
| ρl | 900.48 | kg/m3 | 293.15 | Liquid-... |
| ρl | 900.88 | kg/m3 | 293.15 | Volumet... |
| ρl | 900.26 | kg/m3 | 293.15 | Volumet... |
| ρl | 900.57 | kg/m3 | 293.20 | Liquid-... |
| ρl | 894.40 | kg/m3 | 298.15 | Apparen... |
| ρl | 894.70 | kg/m3 | 298.15 | Ternary... |
| ρl | 897.72 | kg/m3 | 298.15 | Effect ... |
| ρl | 894.37 | kg/m3 | 298.15 | Density... |
| ρl | 894.36 | kg/m3 | 298.15 | Liquid-... |
| ρl | 894.40 | kg/m3 | 298.15 | Measure... |
| ρl | 893.40 | kg/m3 | 298.15 | Solubil... |
| ρl | 894.50 | kg/m3 | 298.15 | (Liquid... |
| ρl | 894.40 | kg/m3 | 298.15 | Revisio... |
| ρl | 894.40 | kg/m3 | 298.15 | Liquid-... |
| ρl | 894.79 | kg/m3 | 298.15 | Volumet... |
| ρl | 894.60 | kg/m3 | 298.15 | Experim... |
| ρl | 894.14 | kg/m3 | 298.15 | Volumet... |
| ρl | 894.47 | kg/m3 | 298.15 | Study o... |
| ρl | 894.51 | kg/m3 | 298.15 | Standar... |
| ρl | 894.38 | kg/m3 | 298.15 | Excess ... |
| ρl | 899.50 | kg/m3 | 298.15 | Isobari... |
| ρl | 893.90 | kg/m3 | 298.40 | Vapor L... |
| ρl | 888.35 | kg/m3 | 303.15 | Study o... |
| ρl | 888.75 | kg/m3 | 303.15 | Excess ... |
| ρl | 888.66 | kg/m3 | 303.15 | Volumet... |
| ρl | 888.26 | kg/m3 | 303.15 | Density... |
| ρl | 888.50 | kg/m3 | 303.15 | Ternary... |
| ρl | 887.85 | kg/m3 | 303.15 | Volumet... |
| ρl | 888.50 | kg/m3 | 303.15 | Apparen... |
| ρl | 888.19 | kg/m3 | 303.15 | Liquid-... |
| ρl | 888.42 | kg/m3 | 303.15 | Studies... |
| ρl | 888.50 | kg/m3 | 303.15 | Volumet... |
| ρl | 888.50 | kg/m3 | 303.15 | Volumet... |
| ρl | 882.48 | kg/m3 | 308.15 | Volumet... |
| ρl | 882.09 | kg/m3 | 308.15 | Density... |
| ρl | 882.70 | kg/m3 | 308.15 | Apparen... |
| ρl | 882.17 | kg/m3 | 308.15 | Study o... |
| ρl | 881.98 | kg/m3 | 308.15 | Liquid-... |
| ρl | 881.52 | kg/m3 | 308.15 | Volumet... |
| ρl | 876.30 | kg/m3 | 313.15 | Apparen... |
| ρl | 876.25 | kg/m3 | 313.15 | Volumet... |
| ρl | 875.81 | kg/m3 | 313.15 | Excess ... |
| ρl | 875.88 | kg/m3 | 313.15 | Density... |
| ρl | 875.95 | kg/m3 | 313.15 | Study o... |
| ρl | 875.73 | kg/m3 | 313.15 | Liquid-... |
| ρl | 875.14 | kg/m3 | 313.15 | Volumet... |
| ρl | 875.10 | kg/m3 | 313.15 | Ternary... |
| ρl | 876.10 | kg/m3 | 313.20 | Liquid-... |
| ρl | 869.62 | kg/m3 | 318.15 | Density... |
| ρl | 869.68 | kg/m3 | 318.15 | Study o... |
| ρl | 863.36 | kg/m3 | 323.15 | Study o... |
| ρl | 863.30 | kg/m3 | 323.15 | Density... |
| ρl | 856.81 | kg/m3 | 328.15 | Excess ... |
| ρl | 851.36 | kg/m3 | 332.70 | Isother... |
| ρl | 843.86 | kg/m3 | 338.15 | Excess ... |
| ρl | 830.62 | kg/m3 | 348.15 | Excess ... |
| ΔfusS | 55.27 | J/mol×K | 189.30 | NIST |
| csound,fluid | [1058.00; 1187.92] | m/s | [288.15; 318.15] |
|
| csound,fluid | 1187.92 | m/s | 288.15 | Densiti... |
| csound,fluid | 1165.80 | m/s | 293.15 | Densiti... |
| csound,fluid | 1143.23 | m/s | 298.15 | Densiti... |
| csound,fluid | 1120.80 | m/s | 303.15 | Densiti... |
| csound,fluid | 1119.00 | m/s | 303.15 | Density... |
| csound,fluid | 1098.43 | m/s | 308.15 | Densiti... |
| csound,fluid | 1098.00 | m/s | 308.15 | Density... |
| csound,fluid | 1081.00 | m/s | 313.15 | Density... |
| csound,fluid | 1058.00 | m/s | 318.15 | Density... |
| γ | [0.02; 0.03] | N/m | [298.15; 323.20] |
|
| γ | 0.02 | N/m | 298.15 | Concent... |
| γ | 0.02 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 323.20 | KDB |
| λ | [0.12; 0.16] | W/m×K | [249.13; 348.46] |
|
| λ | 0.16 | W/m×K | 249.13 | Measure... |
| λ | 0.16 | W/m×K | 253.89 | Measure... |
| λ | 0.16 | W/m×K | 260.17 | Measure... |
| λ | 0.15 | W/m×K | 268.04 | Measure... |
| λ | 0.15 | W/m×K | 274.35 | Measure... |
| λ | 0.15 | W/m×K | 281.34 | Measure... |
| λ | 0.15 | W/m×K | 285.31 | Measure... |
| λ | 0.15 | W/m×K | 290.42 | Measure... |
| λ | 0.14 | W/m×K | 295.44 | Measure... |
| λ | 0.14 | W/m×K | 298.52 | Measure... |
| λ | 0.14 | W/m×K | 303.53 | Measure... |
| λ | 0.14 | W/m×K | 308.44 | Measure... |
| λ | 0.14 | W/m×K | 313.45 | Measure... |
| λ | 0.13 | W/m×K | 318.40 | Measure... |
| λ | 0.13 | W/m×K | 323.25 | Measure... |
| λ | 0.13 | W/m×K | 328.39 | Measure... |
| λ | 0.13 | W/m×K | 333.37 | Measure... |
| λ | 0.13 | W/m×K | 338.34 | Measure... |
| λ | 0.13 | W/m×K | 343.27 | Measure... |
| λ | 0.12 | W/m×K | 345.43 | Measure... |
| λ | 0.12 | W/m×K | 348.46 | Measure... |
Pressure Dependent Properties
| Property | Value | Unit | Pressure (kPa) | Source |
|---|---|---|---|---|
| Tboil | [332.82; 369.50] | K | [54.99; 185.00] |
|
| Tboil | 332.82 | K | 54.99 | Vapor L... |
| Tboil | 335.16 | K | 59.98 | Vapor L... |
| Tboil | 339.42 | K | 70.00 | Vapor L... |
| Tboil | 340.92 | K | 75.00 | Vapor L... |
| Tboil | 343.18 | K | 80.00 | Vapor L... |
| Tboil | 344.93 | K | 84.99 | Vapor L... |
| Tboil | 346.58 | K | 89.91 | Vapor L... |
| Tboil | 348.20 | K | 95.01 | Vapor L... |
| Tboil | 351.26 | K | 104.99 | Vapor L... |
| Tboil | 352.67 | K | 109.98 | Vapor L... |
| Tboil | 355.36 | K | 119.90 | Vapor L... |
| Tboil | 356.62 | K | 124.98 | Vapor L... |
| Tboil | 357.86 | K | 129.93 | Vapor L... |
| Tboil | 359.08 | K | 134.95 | Vapor L... |
| Tboil | 360.24 | K | 139.96 | Vapor L... |
| Tboil | 362.48 | K | 149.95 | Vapor L... |
| Tboil | 363.56 | K | 154.97 | Vapor L... |
| Tboil | 364.60 | K | 159.96 | Vapor L... |
| Tboil | 365.64 | K | 164.99 | Vapor L... |
| Tboil | 367.61 | K | 174.99 | Vapor L... |
| Tboil | 368.58 | K | 180.00 | Vapor L... |
| Tboil | 369.50 | K | 185.00 | Vapor L... |
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 |
|---|---|---|---|---|
| Pvap | [1.33; 202.64] | kPa | [258.37; 372.76] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| 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 | [1.39e-03; 3810.53] | kPa | [189.60; 523.30] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 8.09498e+01 | |||
| Coefficient B | -6.86243e+03 | |||
| Coefficient C | -9.83731e+00 | |||
| Coefficient D | 7.27641e-06 | |||
| 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 |
Similar Compounds
Find more compounds similar to Ethyl Acetate.
Mixtures
- Methane, dibromo- + Ethyl Acetate
- Methane, bromochloro- + Ethyl Acetate
- Ethyl Acetate + Ethane, 1,2-dichloro-
- Ethyl Acetate + Ethane, 1-bromo-2-chloro-
- 1-Butanol + Ethyl Acetate
- Trichloroethylene + Ethyl Acetate
- 1-Butene + Ethyl Acetate
- 2-Butene, (Z)- + Ethyl Acetate
- 2-Butene, (E)- + Ethyl Acetate
- 1-Propene, 2-methyl- + Ethyl Acetate
- Butane + Ethyl Acetate
- Ethyl Acetate + Isobutane
- 1,2-Ethanediol + Ethyl Acetate
- Decane + Ethyl Acetate
- Dodecane + Ethyl Acetate
- Heptane + Ethyl Acetate
- n-Hexane + Ethyl Acetate
- Ethanol + Ethyl Acetate
- Acetic acid + Ethyl Acetate
- Carbon dioxide + Ethanol + Ethyl Acetate
Find more mixtures with Ethyl Acetate.
Sources
- KDB Vapor Pressure Data
- Crippen Method
- 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
- 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
- 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
- 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
- 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
- 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
- Apparent molar volume and apparent molar isentropic compressibility for thebinary systems {methyltrioctylammoniumbis(trifluoromethylsulfonyl)imide + ethyl acetate or ethanol} at different temperatures underatmospheric pressure
- 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
- 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
- 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)
- 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
- 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
- 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
- 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
- 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
- The Yaws Handbook of Vapor Pressure
Note: Cheméo is only indexing the data, follow the source links to retrieve the latest data. The source is also providing more information like the publication year, authors and more.
Take the time to validate and double check the source of the data.
Outlier This icon means
that the value is more than 2 standard deviations away from the
property mean.