- InChI
- InChI=1S/C2H3N/c1-2-3/h1H3
- InChI Key
- WEVYAHXRMPXWCK-UHFFFAOYSA-N
- Formula
- C2H3N
- SMILES
- CC#N
- Molecular Weight1
- 41.05
- CAS
- 75-05-8
- Other Names
-
- Acetonitril
- CH3CN
- Cyanomethane
- Cyanure de methyl
- ETHANENITIRILE
- Ethanenitrile
- Ethanonitrile
- Ethyl nitrile
- Methane, cyano-
- Methanecarbonitrile
- Methyl cyanide
- Methylkyanid
- NA 1648
- NCI-C60822
- Rcra waste number U003
- UN 1648
- USAF EK-488
- 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).
- EA : Electron affinity (eV).
- LFL : Lower Flammability Limit (% in Air).
- UFL : Upper Flammability Limit (% in Air).
- Tflash,cc : Flash Point (Closed Cup Method) (K).
- ΔfG° : Standard Gibbs free energy of formation (kJ/mol).
- Rg : Radius of Gyration.
- ΔfH°gas : Enthalpy of formation at standard conditions (kJ/mol).
- ΔfH°liquid : Liquid phase enthalpy of formation at standard conditions (kJ/mol).
- ΔfusH° : Enthalpy of fusion at standard conditions (kJ/mol).
- ΔfusH : Enthalpy of fusion at a given temperature (kJ/mol).
- ΔvapH° : Enthalpy of vaporization at standard conditions (kJ/mol).
- ΔvapH : Enthalpy of vaporization at a given temperature (kJ/mol).
- IE : Ionization energy (eV).
- log10WS : Log10 of Water solubility in mol/l.
- logPoct/wat : Octanol/Water partition coefficient.
- McVol : McGowan's characteristic volume (ml/mol).
- NFPA Fire : NFPA Fire Rating.
- NFPA Health : NFPA Health Rating.
- NFPA Safety : NFPA Safety Rating.
- Pc : Critical Pressure (kPa).
- Pvap : Vapor pressure (kPa).
- n0 : Refractive Index.
- ρl : Liquid Density (kg/m3).
- Inp : Non-polar retention indices.
- I : Polar retention indices.
- 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).
- ΔvapS : Entropy of vaporization at a given temperature (J/mol×K).
- Tboil : Normal Boiling Point Temperature (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.
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Contents
- Physical Properties
- Temperature Dependent Properties
- Datasets
- Correlations
- Similar Compounds
- Mixtures
- Sources
Physical Properties
| Property | Value | Unit | Source |
|---|---|---|---|
| ω | 0.3270 | KDB | |
| PAff | [779.20; 787.40] | kJ/mol |
|
| PAff | 779.20 | kJ/mol | NIST |
| PAff | 787.40 ± 5.90 | kJ/mol | NIST |
| Tig | 797.04 | K | KDB |
| BasG | 748.00 | kJ/mol | NIST |
| ΔcH°liquid | [-1270.00; -1247.20] | kJ/mol |
|
| ΔcH°liquid | -1256.33 ± 0.30 | kJ/mol | NIST |
| ΔcH°liquid | -1247.20 ± 7.20 | kJ/mol | NIST |
| ΔcH°liquid | -1270.00 | kJ/mol | NIST |
| Cp,liquid | [90.93; 92.36] | J/mol×K |
|
| Cp,liquid | 90.93 | J/mol×K | Heat ca... |
| Cp,liquid | 92.36 | J/mol×K | Volumes... |
| μ | 3.50 | debye | KDB |
| EA | [0.00; 0.01] | eV |
|
| EA | 0.01 | eV | NIST |
| EA | 0.00 ± 0.01 | eV | NIST |
| EA | 0.01 | eV | NIST |
| LFL | 4.40 | % in Air | KDB |
| UFL | 16.00 | % in Air | KDB |
| Tflash,cc | 278.71 | K | KDB |
| ΔfG° | 105.70 | kJ/mol | KDB |
| Rg | 1.8210 | KDB | |
| ΔfH°gas | [65.86; 87.92] | kJ/mol |
|
| ΔfH°gas | 87.92 | kJ/mol | KDB |
| ΔfH°gas | 74.04 ± 0.37 | kJ/mol | NIST |
| ΔfH°gas | 65.86 | kJ/mol | NIST |
| ΔfH°liquid | [31.40; 40.56] | kJ/mol |
|
| ΔfH°liquid | 40.56 ± 0.40 | kJ/mol | NIST |
| ΔfH°liquid | 31.40 | kJ/mol | NIST |
| ΔfusH° | 2.44 | kJ/mol | Joback Calculated Property |
| ΔvapH° | [32.94; 33.45] | kJ/mol |
|
| ΔvapH° | 33.40 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 33.45 ± 0.21 | kJ/mol | NIST |
| ΔvapH° | 33.00 | kJ/mol | NIST |
| ΔvapH° | 32.94 ± 0.06 | kJ/mol | NIST |
| IE | [12.12; 16.98] | eV |
|
| IE | 12.20 ± 0.01 | eV | NIST |
| IE | 12.20 ± 0.00 | eV | NIST |
| IE | 12.38 ± 0.04 | eV | NIST |
| IE | 12.30 ± 0.25 | eV | NIST |
| IE | 12.33 ± 0.08 | eV | NIST |
| IE | 12.19 ± 0.01 | eV | NIST |
| IE | 12.21 | eV | NIST |
| IE | 12.20 ± 0.01 | eV | NIST |
| IE | 13.14 | eV | NIST |
| IE | 15.11 | eV | NIST |
| IE | 12.12 | eV | NIST |
| IE | 13.11 | eV | NIST |
| IE | 15.12 | eV | NIST |
| IE | Outlier 16.98 | eV | NIST |
| IE | 12.19 ± 0.01 | eV | NIST |
| IE | 12.23 ± 0.05 | eV | NIST |
| IE | 12.21 ± 0.00 | eV | NIST |
| IE | 12.22 ± 0.01 | eV | NIST |
| IE | 12.46 | eV | NIST |
| IE | 12.20 | eV | NIST |
| log10WS | [0.26; 0.26] |
|
|
| log10WS | 0.26 | Aq. Sol... | |
| log10WS | 0.26 | Estimat... | |
| logPoct/wat | 0.530 | Crippen Calculated Property | |
| McVol | 40.420 | ml/mol | McGowan Calculated Property |
| NFPA Fire | 3 | KDB | |
| NFPA Health | 2 | KDB | |
| NFPA Safety | 1 | KDB | |
| Pc | [4830.00; 4934.00] | kPa |
|
| Pc | 4850.00 | kPa | KDB |
| Pc | 4890.00 ± 10.00 | kPa | NIST |
| Pc | 4830.00 ± 20.00 | kPa | NIST |
| Pc | 4830.00 ± 20.00 | kPa | NIST |
| Pc | 4934.00 ± 20.00 | kPa | NIST |
| Pc | 4934.00 ± 3.00 | kPa | NIST |
| Pc | 4934.00 ± 3.00 | kPa | NIST |
| Pc | 4830.00 ± 81.06 | kPa | NIST |
| Pc | 4833.20 ± 81.06 | kPa | NIST |
| Pc | 4833.20 ± 81.06 | kPa | NIST |
| Inp | [425.00; 500.00] |
|
|
| Inp | 452.53 | NIST | |
| Inp | 452.72 | NIST | |
| Inp | 452.90 | NIST | |
| Inp | 453.18 | NIST | |
| Inp | 453.70 | NIST | |
| Inp | 454.45 | NIST | |
| Inp | 455.25 | NIST | |
| Inp | 455.74 | NIST | |
| Inp | 456.69 | NIST | |
| Inp | 457.67 | NIST | |
| Inp | 455.45 | NIST | |
| Inp | 454.52 | NIST | |
| Inp | 453.90 | NIST | |
| Inp | 453.32 | NIST | |
| Inp | 452.92 | NIST | |
| Inp | 452.71 | NIST | |
| Inp | 452.50 | NIST | |
| Inp | 452.35 | NIST | |
| Inp | 456.90 | NIST | |
| Inp | 432.00 | NIST | |
| Inp | 442.00 | NIST | |
| Inp | 450.00 | NIST | |
| Inp | 460.00 | NIST | |
| Inp | 464.00 | NIST | |
| Inp | Outlier 425.00 | NIST | |
| Inp | 440.00 | NIST | |
| Inp | 460.00 | NIST | |
| Inp | 444.00 | NIST | |
| Inp | 447.00 | NIST | |
| Inp | 439.00 | NIST | |
| Inp | 439.00 | NIST | |
| Inp | 446.00 | NIST | |
| Inp | Outlier 500.00 | NIST | |
| Inp | 456.00 | NIST | |
| Inp | 470.00 | NIST | |
| Inp | 447.00 | NIST | |
| Inp | 443.00 | NIST | |
| Inp | 452.00 | NIST | |
| Inp | 467.00 | NIST | |
| Inp | 443.00 | NIST | |
| Inp | 455.00 | NIST | |
| Inp | Outlier 490.00 | NIST | |
| Inp | 464.00 | NIST | |
| Inp | 455.00 | NIST | |
| Inp | 447.00 | NIST | |
| Inp | 455.00 | NIST | |
| Inp | 439.00 | NIST | |
| I | [988.00; 1045.00] |
|
|
| I | 1045.00 | NIST | |
| I | 1025.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1030.00 | NIST | |
| I | 1003.00 | NIST | |
| I | 988.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1013.00 | NIST | |
| I | 1002.00 | NIST | |
| I | 1011.00 | NIST | |
| I | 1045.00 | NIST | |
| I | 1010.00 | NIST | |
| I | 1012.00 | NIST | |
| I | 1026.00 | NIST | |
| I | 1045.00 | NIST | |
| S°liquid | 149.62 | J/mol×K | NIST |
| Tboil | [351.00; 370.55] | K |
|
| Tboil | 354.80 | K | KDB |
| Tboil | 354.65 | K | The iso... |
| Tboil | 354.65 | K | (Vapour... |
| Tboil | 354.68 | K | Measure... |
| Tboil | 354.25 | K | Vapor L... |
| Tboil | 354.70 | K | Acetoni... |
| Tboil | 354.74 | K | Isobari... |
| Tboil | 354.65 | K | Vapor-L... |
| Tboil | 354.75 | K | Isobari... |
| Tboil | 354.75 ± 0.20 | K | NIST |
| Tboil | 354.80 | K | NIST |
| Tboil | 354.25 ± 0.30 | K | NIST |
| Tboil | 355.00 | K | NIST |
| Tboil | 354.60 ± 0.30 | K | NIST |
| Tboil | 354.25 ± 0.50 | K | NIST |
| Tboil | Outlier 370.55 ± 0.10 | K | NIST |
| Tboil | 354.70 | K | NIST |
| Tboil | 354.75 ± 0.50 | K | NIST |
| Tboil | 354.70 | K | NIST |
| Tboil | 354.80 ± 0.40 | K | NIST |
| Tboil | 354.80 ± 0.50 | K | NIST |
| Tboil | 354.75 ± 0.20 | K | NIST |
| Tboil | 354.80 ± 0.30 | K | NIST |
| Tboil | 354.75 | K | NIST |
| Tboil | 354.45 ± 0.50 | K | NIST |
| Tboil | 354.65 ± 0.50 | K | NIST |
| Tboil | 354.80 ± 0.30 | K | NIST |
| Tboil | 355.00 ± 0.50 | K | NIST |
| Tboil | 351.00 ± 3.00 | K | NIST |
| Tboil | 354.71 ± 0.20 | K | NIST |
| Tboil | 354.35 ± 0.50 | K | NIST |
| Tboil | 354.70 ± 2.00 | K | NIST |
| Tboil | 355.00 ± 1.50 | K | NIST |
| Tboil | 354.72 ± 0.10 | K | NIST |
| Tboil | 355.00 ± 2.00 | K | NIST |
| Tboil | 355.00 ± 0.50 | K | NIST |
| Tboil | 354.90 ± 0.30 | K | NIST |
| Tboil | 354.70 ± 2.00 | K | NIST |
| Tboil | 355.15 ± 1.50 | K | NIST |
| Tboil | 354.80 ± 0.50 | K | NIST |
| Tboil | 354.00 ± 2.00 | K | NIST |
| Tboil | 355.00 ± 2.00 | K | NIST |
| Tboil | 354.90 ± 0.70 | K | NIST |
| Tboil | 353.00 ± 2.00 | K | NIST |
| Tboil | 355.00 ± 2.00 | K | NIST |
| Tboil | 353.90 ± 1.50 | K | NIST |
| Tboil | 354.80 ± 0.30 | K | NIST |
| Tboil | 354.80 ± 0.30 | K | NIST |
| Tboil | 354.90 ± 0.20 | K | NIST |
| Tboil | 354.80 ± 0.30 | K | NIST |
| Tboil | 354.80 ± 0.60 | K | NIST |
| Tboil | 354.80 ± 0.40 | K | NIST |
| Tboil | 354.75 ± 0.30 | K | NIST |
| Tboil | 354.95 ± 1.50 | K | NIST |
| Tboil | 354.75 ± 0.30 | K | NIST |
| Tboil | 354.70 ± 0.40 | K | NIST |
| Tboil | 354.75 ± 0.20 | K | NIST |
| Tboil | 355.00 ± 1.50 | K | NIST |
| Tboil | 354.69 ± 0.30 | K | NIST |
| Tboil | 354.90 ± 0.60 | K | NIST |
| Tboil | 354.69 ± 0.50 | K | NIST |
| Tc | [543.15; 545.50] | K |
|
| Tc | 545.50 | K | KDB |
| Tc | 545.50 ± 0.20 | K | NIST |
| Tc | 545.50 ± 0.30 | K | NIST |
| Tc | 545.50 ± 0.30 | K | NIST |
| Tc | 544.99 ± 0.20 | K | NIST |
| Tc | 544.99 ± 0.20 | K | NIST |
| Tc | 544.99 ± 0.20 | K | NIST |
| Tc | 543.20 ± 2.00 | K | NIST |
| Tc | 543.45 ± 1.00 | K | NIST |
| Tc | 543.15 ± 1.00 | K | NIST |
| Tfus | [227.45; 230.42] | K |
|
| Tfus | 227.45 | K | Aq. Sol... |
| Tfus | 229.32 | K | KDB |
| Tfus | 229.07 | K | Efficie... |
| Tfus | 230.42 | K | Experim... |
| Ttriple | 229.32 ± 0.02 | K | NIST |
| Vc | 0.173 | m3/kmol | KDB |
| Zc | 0.1849930 | KDB | |
| Zra | 0.20 | KDB |
Temperature Dependent Properties
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Cp,gas | [56.48; 72.87] | J/mol×K | [347.24; 541.37] |
|
|
T(K) Ideal gas heat capacity (J/mol×K) 55 60 65 70 350 400 450 500 | ||||
| Cp,gas | 56.48 | J/mol×K | 347.24 | Joback Calculated Property |
| Cp,gas | 59.46 | J/mol×K | 379.59 | Joback Calculated Property |
| Cp,gas | 62.33 | J/mol×K | 411.95 | Joback Calculated Property |
| Cp,gas | 65.11 | J/mol×K | 444.30 | Joback Calculated Property |
| Cp,gas | 67.79 | J/mol×K | 476.66 | Joback Calculated Property |
| Cp,gas | 70.38 | J/mol×K | 509.01 | Joback Calculated Property |
| Cp,gas | 72.87 | J/mol×K | 541.37 | Joback Calculated Property |
| Cp,liquid | [77.40; 92.82] | J/mol×K | [297.00; 313.15] |
|
|
T(K) Liquid phase heat capacity (J/mol×K) 80 85 90 300 305 310 | ||||
| Cp,liquid | 82.50 | J/mol×K | 297.00 | NIST |
| Cp,liquid | 91.69 | J/mol×K | 298.15 | Volumet... |
| Cp,liquid | 91.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 91.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 91.70 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 77.40 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 91.69 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 91.46 | J/mol×K | 298.15 | NIST |
| Cp,liquid | 81.80 | J/mol×K | 303.15 | NIST |
| Cp,liquid | 92.21 | J/mol×K | 303.15 | Volumet... |
| Cp,liquid | 92.40 | J/mol×K | 308.15 | Volumet... |
| Cp,liquid | 92.82 | J/mol×K | 313.15 | Volumet... |
| η | [0.0002267; 0.0003900] | Pa×s | [293.15; 343.15] |
|
|
T(K) Dynamic viscosity (Pa×s) 2.50e-4 3.00e-4 3.50e-4 4.00e-4 300 320 340 | ||||
| η | 0.0003081 | Pa×s | 293.15 | Thermod... |
| η | 0.0003860 | Pa×s | 293.15 | Viscosi... |
| η | 0.0003900 | Pa×s | 293.15 | Viscosi... |
| η | 0.0003440 | Pa×s | 298.15 | Viscosi... |
| η | 0.0003700 | Pa×s | 298.15 | Propert... |
| η | 0.0003443 | Pa×s | 298.15 | Studies... |
| η | 0.0003431 | Pa×s | 298.15 | Volumet... |
| η | 0.0002857 | Pa×s | 298.15 | Thermod... |
| η | 0.0003696 | Pa×s | 298.15 | Molecul... |
| η | 0.0003417 | Pa×s | 298.15 | Density... |
| η | 0.0003417 | Pa×s | 298.15 | The (wa... |
| η | 0.0003700 | Pa×s | 298.15 | Viscosi... |
| η | 0.0003700 | Pa×s | 298.15 | Viscosi... |
| η | 0.0003540 | Pa×s | 303.15 | Viscosi... |
| η | 0.0003280 | Pa×s | 303.15 | Density... |
| η | 0.0002642 | Pa×s | 303.15 | Thermod... |
| η | 0.0003540 | Pa×s | 303.15 | Propert... |
| η | 0.0003554 | Pa×s | 303.15 | Molecul... |
| η | 0.0003500 | Pa×s | 303.15 | Viscosi... |
| η | 0.0003280 | Pa×s | 303.15 | The (wa... |
| η | 0.0003129 | Pa×s | 308.15 | Density... |
| η | 0.0003414 | Pa×s | 308.15 | Molecul... |
| η | 0.0003130 | Pa×s | 308.15 | Viscosi... |
| η | 0.0002444 | Pa×s | 308.15 | Thermod... |
| η | 0.0003171 | Pa×s | 308.15 | Volumet... |
| η | 0.0003125 | Pa×s | 308.15 | Electri... |
| η | 0.0003124 | Pa×s | 308.15 | Studies... |
| η | 0.0003129 | Pa×s | 308.15 | The (wa... |
| η | 0.0002374 | Pa×s | 310.15 | Thermod... |
| η | 0.0003270 | Pa×s | 313.15 | Propert... |
| η | 0.0003300 | Pa×s | 313.15 | Viscosi... |
| η | 0.0003042 | Pa×s | 313.15 | Electri... |
| η | 0.0003009 | Pa×s | 313.15 | Density... |
| η | 0.0003270 | Pa×s | 313.15 | Viscosi... |
| η | 0.0003009 | Pa×s | 313.15 | The (wa... |
| η | 0.0002267 | Pa×s | 313.15 | Thermod... |
| η | 0.0002899 | Pa×s | 318.15 | The (wa... |
| η | 0.0002918 | Pa×s | 318.15 | Volumet... |
| η | 0.0002903 | Pa×s | 318.15 | Electri... |
| η | 0.0002891 | Pa×s | 318.15 | Studies... |
| η | 0.0002890 | Pa×s | 318.15 | Viscosi... |
| η | 0.0002899 | Pa×s | 318.15 | Density... |
| η | 0.0002890 | Pa×s | 318.15 | Studies... |
| η | 0.0003000 | Pa×s | 323.15 | Viscosi... |
| η | 0.0003020 | Pa×s | 323.15 | Viscosi... |
| η | 0.0003020 | Pa×s | 323.15 | Propert... |
| η | 0.0002680 | Pa×s | 328.15 | Volumet... |
| η | 0.0002810 | Pa×s | 333.15 | Viscosi... |
| η | 0.0002800 | Pa×s | 333.15 | Viscosi... |
| η | 0.0002810 | Pa×s | 333.15 | Propert... |
| η | 0.0002620 | Pa×s | 343.15 | Propert... |
| η | 0.0002620 | Pa×s | 343.15 | Viscosi... |
| η | 0.0002600 | Pa×s | 343.15 | Viscosi... |
| ΔfusH | 8.17 | kJ/mol | 229.30 | NIST |
| ΔvapH | [29.75; 34.80] | kJ/mol | [290.00; 354.70] |
|
|
T(K) Enthalpy of vaporization at a given temperature (kJ/mol) 30 31 32 33 34 35 300 320 340 | ||||
| ΔvapH | 33.90 | kJ/mol | 290.00 | NIST |
| ΔvapH | 34.20 | kJ/mol | 298.00 | NIST |
| ΔvapH | 33.23 | kJ/mol | 298.15 | NIST |
| ΔvapH | 34.80 | kJ/mol | 321.00 | NIST |
| ΔvapH | 33.80 | kJ/mol | 325.00 | NIST |
| ΔvapH | 33.30 | kJ/mol | 334.50 | NIST |
| ΔvapH | 31.38 | kJ/mol | 352.80 | KDB |
| ΔvapH | 29.75 | kJ/mol | 354.70 | NIST |
| Pvap | [4.32; 4174.61] | kPa | [277.92; 535.03] |
|
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 300 400 500 | ||||
| Pvap | 4.32 | kPa | 277.92 | Vapor P... |
| Pvap | 4.49 | kPa | 278.62 | Vapor P... |
| Pvap | 4.44 | kPa | 278.72 | Vapor p... |
| Pvap | 4.54 | kPa | 278.88 | Vapor p... |
| Pvap | 4.51 | kPa | 278.98 | Vapor p... |
| Pvap | 4.73 | kPa | 279.81 | Vapor p... |
| Pvap | 4.86 | kPa | 280.27 | Vapor p... |
| Pvap | 5.25 | kPa | 281.57 | Vapor P... |
| Pvap | 5.34 | kPa | 281.91 | Vapor p... |
| Pvap | 5.64 | kPa | 283.17 | Vapor p... |
| Pvap | 5.84 | kPa | 283.56 | Vapor p... |
| Pvap | 5.92 | kPa | 283.81 | Vapor p... |
| Pvap | 6.10 | kPa | 284.56 | Vapor p... |
| Pvap | 6.38 | kPa | 285.38 | Vapor P... |
| Pvap | 6.47 | kPa | 285.70 | Vapor p... |
| Pvap | 6.59 | kPa | 286.17 | Vapor p... |
| Pvap | 6.75 | kPa | 286.61 | Vapor p... |
| Pvap | 7.17 | kPa | 287.67 | Vapor P... |
| Pvap | 7.50 | kPa | 288.72 | Vapor p... |
| Pvap | 7.56 | kPa | 288.80 | Vapor p... |
| Pvap | 7.59 | kPa | 288.83 | Vapor p... |
| Pvap | 7.80 | kPa | 289.39 | Vapor p... |
| Pvap | 8.03 | kPa | 290.09 | Vapor p... |
| Pvap | 8.30 | kPa | 290.60 | Vapor p... |
| Pvap | 8.30 | kPa | 290.65 | Vapor P... |
| Pvap | 8.60 | kPa | 291.36 | Vapor p... |
| Pvap | 9.16 | kPa | 292.48 | Vapor p... |
| Pvap | 9.18 | kPa | 292.75 | Vapor P... |
| Pvap | 9.41 | kPa | 293.21 | Vapor p... |
| Pvap | 9.82 | kPa | 293.92 | Vapor p... |
| Pvap | 10.03 | kPa | 294.40 | Vapor p... |
| Pvap | 10.00 | kPa | 295.25 | Phase B... |
| Pvap | 10.43 | kPa | 295.33 | Vapor p... |
| Pvap | 10.00 | kPa | 295.40 | Phase B... |
| Pvap | 10.60 | kPa | 295.78 | Vapor P... |
| Pvap | 10.77 | kPa | 295.94 | Vapor p... |
| Pvap | 11.02 | kPa | 296.44 | Vapor p... |
| Pvap | 11.60 | kPa | 297.48 | Vapor p... |
| Pvap | 12.05 | kPa | 298.30 | Vapor p... |
| Pvap | 12.17 | kPa | 298.67 | Vapor p... |
| Pvap | 12.61 | kPa | 299.42 | Vapor p... |
| Pvap | 13.37 | kPa | 300.82 | Vapor P... |
| Pvap | 13.61 | kPa | 301.19 | Vapor p... |
| Pvap | 14.18 | kPa | 302.14 | Vapor p... |
| Pvap | 14.15 | kPa | 302.25 | Vapor-L... |
| Pvap | 15.27 | kPa | 303.81 | Vapor P... |
| Pvap | 15.57 | kPa | 304.16 | Vapor p... |
| Pvap | 16.10 | kPa | 305.01 | Vapor p... |
| Pvap | 16.47 | kPa | 305.51 | Experim... |
| Pvap | 16.96 | kPa | 306.04 | Vapor p... |
| Pvap | 17.53 | kPa | 306.90 | Vapor p... |
| Pvap | 17.52 | kPa | 307.09 | Vapor-L... |
| Pvap | 18.22 | kPa | 307.95 | Vapor p... |
| Pvap | 18.59 | kPa | 308.32 | Vapor L... |
| Pvap | 19.64 | kPa | 309.64 | Vapor P... |
| Pvap | 19.85 | kPa | 309.92 | Vapor p... |
| Pvap | 20.49 | kPa | 310.71 | Vapor p... |
| Pvap | 21.13 | kPa | 311.49 | Vapor-L... |
| Pvap | 21.38 | kPa | 311.79 | Vapor p... |
| Pvap | 21.55 | kPa | 311.88 | Vapor p... |
| Pvap | 22.50 | kPa | 312.81 | Vapor p... |
| Pvap | 22.65 | kPa | 313.15 | Vapor-L... |
| Pvap | 23.42 | kPa | 313.77 | Vapor p... |
| Pvap | 24.17 | kPa | 314.79 | Vapor p... |
| Pvap | 24.97 | kPa | 315.43 | Vapor P... |
| Pvap | 25.10 | kPa | 315.71 | Vapor p... |
| Pvap | 25.15 | kPa | 315.79 | Vapor p... |
| Pvap | 25.72 | kPa | 316.27 | Vapor-L... |
| Pvap | 26.11 | kPa | 316.63 | Vapor p... |
| Pvap | 27.19 | kPa | 317.53 | Vapor L... |
| Pvap | 27.21 | kPa | 317.72 | Vapor p... |
| Pvap | 27.78 | kPa | 318.18 | Vapor-L... |
| Pvap | 28.27 | kPa | 318.66 | Vapor p... |
| Pvap | 29.39 | kPa | 319.69 | Vapor p... |
| Pvap | 30.64 | kPa | 320.65 | Vapor-L... |
| Pvap | 30.52 | kPa | 320.67 | Vapor p... |
| Pvap | 31.31 | kPa | 321.12 | Vapor P... |
| Pvap | 31.73 | kPa | 321.65 | Vapor p... |
| Pvap | 32.95 | kPa | 322.54 | Vapor p... |
| Pvap | 32.94 | kPa | 322.56 | Vapor p... |
| Pvap | 33.19 | kPa | 322.64 | Vapor p... |
| Pvap | 33.71 | kPa | 323.12 | Experim... |
| Pvap | 33.86 | kPa | 323.15 | Vapor P... |
| Pvap | 33.80 | kPa | 323.16 | Vapor-L... |
| Pvap | 34.49 | kPa | 323.64 | Vapor p... |
| Pvap | 35.65 | kPa | 324.59 | Vapor p... |
| Pvap | 36.39 | kPa | 325.02 | Vapor P... |
| Pvap | 37.00 | kPa | 325.58 | Vapor p... |
| Pvap | 37.80 | kPa | 326.03 | Vapor L... |
| Pvap | 37.90 | kPa | 326.16 | Vapor-L... |
| Pvap | 41.38 | kPa | 328.50 | Vapor-L... |
| Pvap | 43.71 | kPa | 329.94 | Vapor L... |
| Pvap | 45.62 | kPa | 331.15 | Vapor-L... |
| Pvap | 45.91 | kPa | 331.27 | Vapor P... |
| Pvap | 49.06 | kPa | 333.15 | Vapor-L... |
| Pvap | 49.16 | kPa | 333.15 | Vapor-L... |
| Pvap | 49.76 | kPa | 333.51 | Vapor L... |
| Pvap | 49.76 | kPa | 333.57 | Vapor L... |
| Pvap | 54.01 | kPa | 335.84 | Vapor-L... |
| Pvap | 55.17 | kPa | 336.41 | Vapor P... |
| Pvap | 55.46 | kPa | 336.56 | Vapor L... |
| Pvap | 58.58 | kPa | 338.15 | Vapor-L... |
| Pvap | 60.76 | kPa | 339.20 | Vapor L... |
| Pvap | 64.81 | kPa | 341.07 | Vapor L... |
| Pvap | 65.07 | kPa | 341.18 | Vapor P... |
| Pvap | 69.62 | kPa | 343.18 | Vapor-L... |
| Pvap | 71.24 | kPa | 343.86 | Vapor L... |
| Pvap | 71.24 | kPa | 343.94 | Vapor L... |
| Pvap | 75.44 | kPa | 345.57 | Vapor P... |
| Pvap | 75.40 | kPa | 345.58 | Vapor L... |
| Pvap | 80.49 | kPa | 347.55 | Vapor L... |
| Pvap | 82.37 | kPa | 348.25 | Vapor-L... |
| Pvap | 85.31 | kPa | 349.33 | Vapor P... |
| Pvap | 86.34 | kPa | 349.69 | Vapor L... |
| Pvap | 92.16 | kPa | 351.76 | Vapor L... |
| Pvap | 95.59 | kPa | 352.88 | Vapor P... |
| Pvap | 96.34 | kPa | 353.10 | Vapor-L... |
| Pvap | 96.17 | kPa | 353.13 | Experim... |
| Pvap | 99.40 | kPa | 354.12 | Vapor L... |
| Pvap | 101.32 | kPa | 354.25 | Vapor L... |
| Pvap | 100.75 | kPa | 354.55 | Vapor P... |
| Pvap | 101.30 | kPa | 354.65 | The iso... |
| Pvap | 101.12 | kPa | 354.67 | Vapor P... |
| Pvap | 101.32 | kPa | 354.70 | Acetoni... |
| Pvap | 101.30 | kPa | 354.74 | Isobari... |
| Pvap | 101.30 | kPa | 354.75 | Isobari... |
| Pvap | 110.61 | kPa | 357.56 | Vapor P... |
| Pvap | 122.63 | kPa | 360.94 | Vapor P... |
| Pvap | 125.13 | kPa | 361.61 | Vapor P... |
| Pvap | 131.21 | kPa | 363.15 | Vapor-L... |
| Pvap | 155.33 | kPa | 368.97 | Vapor P... |
| Pvap | 168.12 | kPa | 371.74 | Vapor P... |
| Pvap | 175.04 | kPa | 373.17 | Vapor P... |
| Pvap | 204.59 | kPa | 378.81 | Vapor P... |
| Pvap | 235.79 | kPa | 384.11 | Vapor P... |
| Pvap | 297.37 | kPa | 393.15 | Vapor-L... |
| Pvap | 306.28 | kPa | 394.29 | Vapor P... |
| Pvap | 399.50 | kPa | 405.24 | Vapor P... |
| Pvap | 502.67 | kPa | 415.21 | Vapor P... |
| Pvap | 605.60 | kPa | 423.68 | Vapor P... |
| Pvap | 708.99 | kPa | 431.12 | Vapor P... |
| Pvap | 804.86 | kPa | 437.30 | Vapor P... |
| Pvap | 910.82 | kPa | 443.50 | Vapor P... |
| Pvap | 1025.47 | kPa | 449.60 | Vapor P... |
| Pvap | 1096.90 | kPa | 453.15 | Vapor-L... |
| Pvap | 1151.97 | kPa | 455.74 | Vapor P... |
| Pvap | 1290.20 | kPa | 461.87 | Vapor P... |
| Pvap | 1450.28 | kPa | 468.37 | Vapor P... |
| Pvap | 1602.63 | kPa | 474.05 | Vapor P... |
| Pvap | 1749.84 | kPa | 479.15 | Vapor P... |
| Pvap | 1923.88 | kPa | 484.77 | Vapor P... |
| Pvap | 2110.77 | kPa | 490.37 | Vapor P... |
| Pvap | 2303.51 | kPa | 495.75 | Vapor P... |
| Pvap | 2523.66 | kPa | 501.48 | Vapor P... |
| Pvap | 2747.95 | kPa | 506.92 | Vapor P... |
| Pvap | 2999.22 | kPa | 512.61 | Vapor P... |
| Pvap | 3254.08 | kPa | 518.01 | Vapor P... |
| Pvap | 3512.89 | kPa | 523.15 | Vapor P... |
| Pvap | 3760.37 | kPa | 527.79 | Vapor P... |
| Pvap | 4001.46 | kPa | 532.08 | Vapor P... |
| Pvap | 4174.61 | kPa | 535.03 | Vapor P... |
| n0 | [1.33710; 1.35900] | [293.15; 308.15] |
|
|
|
T(K) Refractive Index 1.34 1.34 1.35 1.35 1.36 1.36 295 300 305 | ||||
| n0 | 1.34390 | 293.15 | A novel... | |
| n0 | 1.34420 | 293.15 | ERAS mo... | |
| n0 | 1.34386 | 293.15 | Ternary... | |
| n0 | 1.34250 | 293.15 | Isobari... | |
| n0 | 1.34410 | 293.15 | Experim... | |
| n0 | 1.34300 | 293.15 | Solubil... | |
| n0 | 1.34390 | 293.15 | Experim... | |
| n0 | 1.34360 | 293.15 | Densiti... | |
| n0 | 1.34300 | 293.15 | Solubil... | |
| n0 | 1.34410 | 295.10 | Ternary... | |
| n0 | 1.34139 | 298.15 | Isother... | |
| n0 | 1.34190 | 298.15 | Viscosi... | |
| n0 | 1.34180 | 298.15 | Physics... | |
| n0 | 1.34180 | 298.15 | Vapor-L... | |
| n0 | 1.34110 | 298.15 | Densiti... | |
| n0 | 1.35900 | 298.15 | Volumet... | |
| n0 | 1.34160 | 298.15 | (Vapor ... | |
| n0 | 1.34160 | 298.15 | Acousti... | |
| n0 | 1.34160 | 298.15 | Excess ... | |
| n0 | 1.33900 | 303.15 | Densiti... | |
| n0 | 1.33960 | 303.15 | Liquid ... | |
| n0 | 1.33710 | 308.15 | Densiti... | |
| ρl | [726.43; 798.12] | kg/m3 | [278.15; 343.15] |
|
|
T(K) Liquid Density (kg/m3) 720 740 760 780 800 280 300 320 340 | ||||
| ρl | 798.12 | kg/m3 | 278.15 | Thermod... |
| ρl | 792.79 | kg/m3 | 283.15 | Thermod... |
| ρl | 787.31 | kg/m3 | 288.13 | Thermod... |
| ρl | 787.31 | kg/m3 | 288.13 | Thermod... |
| ρl | 787.31 | kg/m3 | 288.13 | Thermod... |
| ρl | 787.38 | kg/m3 | 288.15 | Volumet... |
| ρl | 787.39 | kg/m3 | 288.15 | Density... |
| ρl | 787.31 | kg/m3 | 288.15 | Thermod... |
| ρl | 787.58 | kg/m3 | 288.15 | The The... |
| ρl | 787.33 | kg/m3 | 288.15 | Density... |
| ρl | 787.44 | kg/m3 | 288.15 | Thermod... |
| ρl | 782.00 | kg/m3 | 293.00 | KDB |
| ρl | 783.38 | kg/m3 | 293.15 | Isobari... |
| ρl | 782.10 | kg/m3 | 293.15 | Effect ... |
| ρl | 782.06 | kg/m3 | 293.15 | Thermod... |
| ρl | 782.10 | kg/m3 | 293.15 | Densiti... |
| ρl | 782.30 | kg/m3 | 293.15 | Densiti... |
| ρl | 781.89 | kg/m3 | 293.15 | Volumet... |
| ρl | 782.12 | kg/m3 | 293.15 | Densiti... |
| ρl | 781.93 | kg/m3 | 293.15 | Thermod... |
| ρl | 782.04 | kg/m3 | 293.15 | Volumet... |
| ρl | 781.89 | kg/m3 | 293.15 | The The... |
| ρl | 786.50 | kg/m3 | 293.15 | Interpr... |
| ρl | 782.01 | kg/m3 | 293.15 | Volumet... |
| ρl | 781.96 | kg/m3 | 293.15 | Density... |
| ρl | 782.00 | kg/m3 | 293.15 | Thermop... |
| ρl | 781.93 | kg/m3 | 293.15 | Thermod... |
| ρl | 781.93 | kg/m3 | 293.15 | Thermod... |
| ρl | 781.95 | kg/m3 | 293.15 | Volumet... |
| ρl | 782.00 | kg/m3 | 293.15 | Thermod... |
| ρl | 781.93 | kg/m3 | 293.15 | Thermod... |
| ρl | 782.12 | kg/m3 | 293.15 | Densiti... |
| ρl | 782.10 | kg/m3 | 293.15 | Measure... |
| ρl | 782.01 | kg/m3 | 293.15 | Volumet... |
| ρl | 776.47 | kg/m3 | 298.15 | Solutio... |
| ρl | 776.53 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.61 | kg/m3 | 298.15 | Volumet... |
| ρl | 777.10 | kg/m3 | 298.15 | Solubil... |
| ρl | 777.00 | kg/m3 | 298.15 | Measure... |
| ρl | 776.30 | kg/m3 | 298.15 | Solubil... |
| ρl | 776.62 | kg/m3 | 298.15 | Ionic m... |
| ρl | 776.82 | kg/m3 | 298.15 | Densiti... |
| ρl | 776.53 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.53 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.52 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.53 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.62 | kg/m3 | 298.15 | Calorim... |
| ρl | 776.00 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.74 | kg/m3 | 298.15 | Probing... |
| ρl | 776.55 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.62 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.62 | kg/m3 | 298.15 | Density... |
| ρl | 776.65 | kg/m3 | 298.15 | Densiti... |
| ρl | 776.82 | kg/m3 | 298.15 | Densiti... |
| ρl | 776.71 | kg/m3 | 298.15 | Excess ... |
| ρl | 776.80 | kg/m3 | 298.15 | Densiti... |
| ρl | 776.71 | kg/m3 | 298.15 | Effect ... |
| ρl | 785.71 | kg/m3 | 298.15 | Liquid-... |
| ρl | 776.53 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.69 | kg/m3 | 298.15 | Standar... |
| ρl | 776.64 | kg/m3 | 298.15 | Liquid ... |
| ρl | 776.55 | kg/m3 | 298.15 | Liquid-... |
| ρl | 776.66 | kg/m3 | 298.15 | Thermod... |
| ρl | 776.50 | kg/m3 | 298.15 | Bubble ... |
| ρl | 776.93 | kg/m3 | 298.15 | Densiti... |
| ρl | 776.68 | kg/m3 | 298.15 | Explora... |
| ρl | 776.51 | kg/m3 | 298.15 | Excess ... |
| ρl | 781.10 | kg/m3 | 298.15 | Interpr... |
| ρl | 776.64 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.60 | kg/m3 | 298.15 | Density... |
| ρl | 776.61 | kg/m3 | 298.15 | Density... |
| ρl | 776.53 | kg/m3 | 298.15 | Volumet... |
| ρl | 776.52 | kg/m3 | 298.15 | The The... |
| ρl | 776.85 | kg/m3 | 298.15 | Compres... |
| ρl | 771.12 | kg/m3 | 303.13 | Volumet... |
| ρl | 771.52 | kg/m3 | 303.15 | Densiti... |
| ρl | 773.30 | kg/m3 | 303.15 | Interpr... |
| ρl | 771.44 | kg/m3 | 303.15 | Densiti... |
| ρl | 771.29 | kg/m3 | 303.15 | Excess ... |
| ρl | 771.50 | kg/m3 | 303.15 | Densiti... |
| ρl | 771.13 | kg/m3 | 303.15 | Volumet... |
| ρl | 771.18 | kg/m3 | 303.15 | Density... |
| ρl | 771.19 | kg/m3 | 303.15 | Volumet... |
| ρl | 771.21 | kg/m3 | 303.15 | Volumet... |
| ρl | 768.14 | kg/m3 | 303.15 | Densiti... |
| ρl | 771.56 | kg/m3 | 303.15 | Solutio... |
| ρl | 771.11 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.06 | kg/m3 | 303.15 | Excess ... |
| ρl | 771.23 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.12 | kg/m3 | 303.15 | The The... |
| ρl | 771.10 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.11 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.10 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.20 | kg/m3 | 303.15 | Volumet... |
| ρl | 771.52 | kg/m3 | 303.15 | Densiti... |
| ρl | 771.00 | kg/m3 | 303.15 | Thermod... |
| ρl | 771.29 | kg/m3 | 303.15 | Effect ... |
| ρl | 771.00 | kg/m3 | 303.15 | Thermop... |
| ρl | 771.43 | kg/m3 | 303.15 | Densiti... |
| ρl | 765.98 | kg/m3 | 308.10 | Synthes... |
| ρl | 766.30 | kg/m3 | 308.15 | Densiti... |
| ρl | 766.21 | kg/m3 | 308.15 | Densiti... |
| ρl | 761.45 | kg/m3 | 308.15 | Densiti... |
| ρl | 760.00 | kg/m3 | 308.15 | Densiti... |
| ρl | 765.83 | kg/m3 | 308.15 | Effect ... |
| ρl | 761.40 | kg/m3 | 308.15 | Densiti... |
| ρl | 765.75 | kg/m3 | 308.15 | Volumet... |
| ρl | 765.26 | kg/m3 | 308.15 | Solutio... |
| ρl | 765.64 | kg/m3 | 308.15 | Thermod... |
| ρl | 766.21 | kg/m3 | 308.15 | Densiti... |
| ρl | 765.81 | kg/m3 | 308.15 | Density... |
| ρl | 765.75 | kg/m3 | 308.15 | Volumet... |
| ρl | 765.83 | kg/m3 | 308.15 | Excess ... |
| ρl | 765.68 | kg/m3 | 308.15 | Volumet... |
| ρl | 763.20 | kg/m3 | 308.15 | Densiti... |
| ρl | 765.83 | kg/m3 | 308.15 | The The... |
| ρl | 765.59 | kg/m3 | 308.15 | Excess ... |
| ρl | 765.97 | kg/m3 | 308.15 | Densiti... |
| ρl | 765.66 | kg/m3 | 308.15 | Thermod... |
| ρl | 765.65 | kg/m3 | 308.15 | Thermod... |
| ρl | 765.73 | kg/m3 | 308.15 | Density... |
| ρl | 766.50 | kg/m3 | 308.15 | Interpr... |
| ρl | 765.77 | kg/m3 | 308.15 | Thermod... |
| ρl | 760.16 | kg/m3 | 313.15 | Thermod... |
| ρl | 760.18 | kg/m3 | 313.15 | Thermod... |
| ρl | 760.50 | kg/m3 | 313.15 | Interpr... |
| ρl | 760.16 | kg/m3 | 313.15 | Thermod... |
| ρl | 755.34 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.36 | kg/m3 | 313.15 | The The... |
| ρl | 759.55 | kg/m3 | 313.15 | Solutio... |
| ρl | 760.25 | kg/m3 | 313.15 | Density... |
| ρl | 760.68 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.20 | kg/m3 | 313.15 | Volumet... |
| ρl | 760.34 | kg/m3 | 313.15 | Excess ... |
| ρl | 760.15 | kg/m3 | 313.15 | Thermod... |
| ρl | 760.90 | kg/m3 | 313.15 | Densiti... |
| ρl | 752.52 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.18 | kg/m3 | 313.15 | Volumet... |
| ρl | 752.55 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.00 | kg/m3 | 313.15 | Thermop... |
| ρl | 755.36 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.34 | kg/m3 | 313.15 | Effect ... |
| ρl | 761.00 | kg/m3 | 313.15 | Densiti... |
| ρl | 760.25 | kg/m3 | 313.15 | Volumet... |
| ρl | 760.10 | kg/m3 | 313.15 | Excess ... |
| ρl | 760.90 | kg/m3 | 313.15 | Densiti... |
| ρl | 755.59 | kg/m3 | 318.15 | Densiti... |
| ρl | 755.70 | kg/m3 | 318.15 | Densiti... |
| ρl | 754.73 | kg/m3 | 318.15 | Volumet... |
| ρl | 755.59 | kg/m3 | 318.15 | Densiti... |
| ρl | 755.14 | kg/m3 | 318.15 | The The... |
| ρl | 754.82 | kg/m3 | 318.15 | Effect ... |
| ρl | 754.85 | kg/m3 | 318.15 | Density... |
| ρl | 754.56 | kg/m3 | 318.15 | Excess ... |
| ρl | 754.72 | kg/m3 | 318.15 | Density... |
| ρl | 754.82 | kg/m3 | 318.15 | Excess ... |
| ρl | 749.11 | kg/m3 | 323.15 | Thermod... |
| ρl | 749.07 | kg/m3 | 323.15 | Thermod... |
| ρl | 749.73 | kg/m3 | 323.15 | Densiti... |
| ρl | 749.11 | kg/m3 | 323.15 | Volumet... |
| ρl | 749.25 | kg/m3 | 323.15 | Effect ... |
| ρl | 749.44 | kg/m3 | 323.15 | The The... |
| ρl | 749.16 | kg/m3 | 323.15 | Density... |
| ρl | 748.99 | kg/m3 | 323.15 | Excess ... |
| ρl | 749.07 | kg/m3 | 323.15 | Thermod... |
| ρl | 749.25 | kg/m3 | 323.15 | Excess ... |
| ρl | 749.07 | kg/m3 | 323.15 | Thermod... |
| ρl | 738.19 | kg/m3 | 333.15 | Densiti... |
| ρl | 737.86 | kg/m3 | 333.15 | Volumet... |
| ρl | 726.43 | kg/m3 | 343.15 | Volumet... |
| ρl | 726.94 | kg/m3 | 343.15 | Densiti... |
| csound,fluid | [1198.32; 1319.14] | m/s | [288.15; 318.15] |
|
|
T(K) Speed of sound in fluid (m/s) 1200 1220 1240 1260 1280 1300 1320 290 300 310 | ||||
| csound,fluid | 1319.14 | m/s | 288.15 | Volumet... |
| csound,fluid | 1299.01 | m/s | 293.15 | Volumet... |
| csound,fluid | 1278.62 | m/s | 298.15 | Applica... |
| csound,fluid | 1278.77 | m/s | 298.15 | Volumet... |
| csound,fluid | 1281.30 | m/s | 298.15 | Compres... |
| csound,fluid | 1278.62 | m/s | 298.15 | Volumet... |
| csound,fluid | 1278.28 | m/s | 298.15 | Thermod... |
| csound,fluid | 1258.73 | m/s | 303.15 | Applica... |
| csound,fluid | 1258.51 | m/s | 303.15 | Volumet... |
| csound,fluid | 1258.73 | m/s | 303.15 | Volumet... |
| csound,fluid | 1238.66 | m/s | 308.15 | Applica... |
| csound,fluid | 1239.00 | m/s | 308.15 | Ultraso... |
| csound,fluid | 1238.40 | m/s | 308.15 | Volumet... |
| csound,fluid | 1238.66 | m/s | 308.15 | Volumet... |
| csound,fluid | 1218.52 | m/s | 313.15 | Volumet... |
| csound,fluid | 1218.52 | m/s | 313.15 | Applica... |
| csound,fluid | 1198.32 | m/s | 318.15 | Volumet... |
| csound,fluid | 1198.32 | m/s | 318.15 | Applica... |
| γ | [0.03; 0.03] | N/m | [278.15; 313.15] |
|
|
T(K) Surface Tension (N/m) 0.03 0.03 0.03 0.03 280 290 300 310 | ||||
| γ | 0.03 | N/m | 278.15 | Applica... |
| γ | 0.03 | N/m | 283.15 | Surface... |
| γ | 0.03 | N/m | 283.15 | Applica... |
| γ | 0.03 | N/m | 288.15 | Applica... |
| γ | 0.03 | N/m | 288.15 | Physico... |
| γ | 0.03 | N/m | 293.15 | Applica... |
| γ | 0.03 | N/m | 293.15 | Thermod... |
| γ | 0.03 | N/m | 293.15 | Density... |
| γ | 0.03 | N/m | 293.15 | Surface... |
| γ | 0.03 | N/m | 293.20 | KDB |
| γ | 0.03 | N/m | 298.15 | Experim... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 298.15 | Surface... |
| γ | 0.03 | N/m | 298.15 | Applica... |
| γ | 0.03 | N/m | 298.15 | Physico... |
| γ | 0.03 | N/m | 298.15 | Thermod... |
| γ | 0.03 | N/m | 303.13 | Surface... |
| γ | 0.03 | N/m | 303.15 | Applica... |
| γ | 0.03 | N/m | 303.15 | Thermod... |
| γ | 0.03 | N/m | 308.15 | Applica... |
| γ | 0.03 | N/m | 308.15 | Physico... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 308.15 | Thermod... |
| γ | 0.03 | N/m | 308.15 | Surface... |
| γ | 0.03 | N/m | 313.15 | Applica... |
| γ | 0.03 | N/m | 313.15 | Thermod... |
| γ | 0.03 | N/m | 313.15 | Surface... |
| ΔvapS | 111.44 | J/mol×K | 298.15 | NIST |
| λ | [0.18; 0.21] | W/m×K | [273.15; 313.15] |
|
| λ | 0.21 | W/m×K | 273.15 | Liquid ... |
| λ | 0.20 | W/m×K | 293.15 | Liquid ... |
| λ | 0.18 | W/m×K | 313.15 | Liquid ... |
Datasets
Refractive index (Na D-line)
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Refractive index (Na D-line) - Liquid |
| 81.50 | 298.15 | 1.3417 |
| Reference | ||
Mass density, kg/m3
| Fixed | Measured | |
|---|---|---|
| Pressure, kPa - Liquid | Temperature, K - Liquid | Mass density, kg/m3 - Liquid |
| 200.00 | 313.15 | 755.0 |
| 200.00 | 353.15 | 710.0 |
| 600.00 | 313.15 | 755.0 |
| 600.00 | 353.15 | 711.0 |
| 600.00 | 393.15 | 664.0 |
| 1000.00 | 313.15 | 756.0 |
| 1000.00 | 353.15 | 711.0 |
| 1000.00 | 393.15 | 664.0 |
| 1000.00 | 433.15 | 611.0 |
| 1400.00 | 313.15 | 756.0 |
| 1400.00 | 353.15 | 711.0 |
| 1400.00 | 393.15 | 665.0 |
| 1400.00 | 433.15 | 612.0 |
| 1800.00 | 313.15 | 757.0 |
| 1800.00 | 353.15 | 712.0 |
| 1800.00 | 393.15 | 666.0 |
| 1800.00 | 433.15 | 614.0 |
| 1800.00 | 473.15 | 550.0 |
| 2000.00 | 313.15 | 757.0 |
| 2000.00 | 353.15 | 713.0 |
| 2000.00 | 393.15 | 666.0 |
| 2000.00 | 433.15 | 614.0 |
| 2000.00 | 473.15 | 552.0 |
| Reference | ||
Correlations
| Property | Value | Unit | Temperature (K) | Source |
|---|---|---|---|---|
| Pvap | [0.19; 4818.59] | kPa | [229.32; 545.50] |
The Yaw...
|
| Equation | ln(Pvp) = A + B/(T + C) | |||
| Coefficient A | 1.53562e+01 | |||
| Coefficient B | -3.64591e+03 | |||
| Coefficient C | -1.52630e+01 | |||
| Temperature range, min. | 229.32 | |||
| Temperature range, max. | 545.50 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 0.19 | kPa | 229.32 | Calculated Property |
| Pvap | 2.06 | kPa | 264.45 | Calculated Property |
| Pvap | 12.59 | kPa | 299.58 | Calculated Property |
| Pvap | 51.58 | kPa | 334.71 | Calculated Property |
| Pvap | 159.80 | kPa | 369.84 | Calculated Property |
| Pvap | 403.77 | kPa | 404.98 | Calculated Property |
| Pvap | 875.21 | kPa | 440.11 | Calculated Property |
| Pvap | 1685.66 | kPa | 475.24 | Calculated Property |
| Pvap | 2958.21 | kPa | 510.37 | Calculated Property |
| Pvap | 4818.59 | kPa | 545.50 | Calculated Property |
| Pvap | [0.19; 4811.04] | kPa | [229.32; 545.50] |
KDB Vap...
|
| Equation | ln(Pvp) = A + B/T + C*ln(T) + D*T^2 | |||
| Coefficient A | 4.10590e+01 | |||
| Coefficient B | -4.99962e+03 | |||
| Coefficient C | -3.88171e+00 | |||
| Coefficient D | 3.51596e-06 | |||
| Temperature range, min. | 229.32 | |||
| Temperature range, max. | 545.50 | |||
|
T(K) Vapor pressure (kPa) 0 1000 2000 3000 4000 5000 300 400 500 | ||||
| Pvap | 0.19 | kPa | 229.32 | Calculated Property |
| Pvap | 2.11 | kPa | 264.45 | Calculated Property |
| Pvap | 12.82 | kPa | 299.58 | Calculated Property |
| Pvap | 51.96 | kPa | 334.71 | Calculated Property |
| Pvap | 159.00 | kPa | 369.84 | Calculated Property |
| Pvap | 397.44 | kPa | 404.98 | Calculated Property |
| Pvap | 855.75 | kPa | 440.11 | Calculated Property |
| Pvap | 1646.99 | kPa | 475.24 | Calculated Property |
| Pvap | 2909.58 | kPa | 510.37 | Calculated Property |
| Pvap | 4811.04 | kPa | 545.50 | Calculated Property |
Similar Compounds
Find more compounds similar to Acetonitrile.
Mixtures
- 1-Propanol + Acetonitrile
- Acetonitrile + 1-Hexanol
- Acetonitrile + Butanedioic acid, methylene-
- n-Hexane + Acetonitrile
- Acetonitrile + Methyl Alcohol
- Acetonitrile + Crotonic acid
- Acetonitrile + D-malic acid
- Acetonitrile + Maleic anhydride
- Acetonitrile + Fenofibrate
- Benzene + n-Hexane + Acetonitrile
- Acetonitrile + Dodecane + Acetic acid
- Acetonitrile + Dodecane + Propanoic acid
- Acetonitrile + Dodecane + Butanoic acid
- Acetonitrile + Dodecane + Propanoic acid, 2-methyl-
- Acetonitrile + Dodecane + Pentanoic acid
- Acetonitrile + Dodecane + Butanoic acid, 3-methyl-
- Benzene + Acetonitrile + Hexadecane
- Toluene + Acetonitrile + Hexadecane
- Acetonitrile + p-Xylene + Hexadecane
- Benzene + Acetonitrile
Find more mixtures with Acetonitrile.
Sources
- KDB Pure (Korean Thermophysical Properties Databank)
- KDB Vapor Pressure Data
- Crippen Method
- Dortmund Data Bank Vapor-Liquid Equilibrium Data
- Volumetric Properties of the Ionic Liquid, 1-Butyl-3-methylimidazolium Tetrafluoroborate, in Organic Solvents at T = 298.15 K
- Application of the Extended Langmuir Model for the Determination of Lyophobicity of 1-Propanol in Acetonitrile
- Volumetric and Isentropic Compressibility Behavior of Ionic Liquid, 1-Propyl-3-Methylimidazolium Bromide in Acetonitrile, Dimethylformamide, and Dimethylsulfoxide at T = (288.15 to 308.15) K
- Synthesis of 1,3-Dimethylimidazolium Chloride and Volumetric Property Investigations of Its Aqueous Solution
- Interpretation of Association Behavior and Molecular Interactions in Binary Mixtures from Thermoacoustics and Molecular Compression Data
- Solubility of 9-fluorenone, thianthrene and xanthene in organic solvents
- Liquid liquid equilibria and partitioning in organic aqueous systems
- Measurement and correlation of liquid liquid equilibria for acetonitrile + n-alkane systems
- Osmotic coefficients of some imidazolium based ionic liquids in water and acetonitrile at temperature 318.15K
- Measurement of activity coefficients at infinite dilution for acetonitrile, water, limonene, limonene epoxide and their binary pairs
- Volumetric properties of ionic liquid 1,3-dimethylimidazolium methyl sulfate + molecular solvents at T = (298.15 - 328.15) K
- Bubble point measurements of binary mixtures formed by 1-hexanol with selected nitro-compounds and substituted benzenes at 95.6 kPa
- Activity coefficients at infinite dilution of organic solutes in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Determination and correlation of liquid-liquid equilibria for nine binary acetonitrile + n-alkane systems
- A model for excess volumes of salty water-acetonitrile mixtures at 298.15 K
- Solubility of itaconic acid in different organic solvents: Experimental measurement and thermodynamic modeling
- Solubility of citric, malonic, and malic acids in different solvents from 303.2 to 333.2 K
- Activity coefficients at infinite dilution of organic solutes in 1-octyl-3-methylimidazolium nitrate using gas-liquid chromatography
- Thermodynamic analysis and correlation of solubility of candesartan cilexetil in aqueous solvent mixtures
- A novel static analytical apparatus for phase equilibrium measurements
- Isobaric vapor liquid equilibrium for binary system of methanol and acetonitrile
- Thermodynamics of solubility of thiomalic acid in different organicsolvents from 278.15 K to 333.15 K
- Using binary mixtures of dicationic ionic liquids for determination ofactivity coefficients at infinite dilution by gas-liquid chromatography
- 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
- Ionic interplay of lithium salts in binary mixtures of acetonitrile and diethyl carbonate probed by physicochemical approach
- Solubility of 1, 3, 2-dioxaphosphorinane-5,5-dimethyl -2- (2,4,6-tribromophenoxy)-2-oxide in selected solvents
- Salting-out effect of sodium, potassium, carbonate, sulfite, tartrate and thiosulfate ions on aqueous mixtures of acetonitrile or 1-methyl-2-pyrrolidone: A liquid-liquid equilibrium study
- Determination and correlation of solubilities of 1,2-bis(2-oxo-5,5-dimethyl-1,3,2-dioxyphosphacyclohexyl-2-imino) ethane in selected solvents
- Measurement and correlation solubility and mixing properties of L-malic acid in pure and mixture organic solvents
- Measurement and correlation of the solubility of maleic anhydride in different organic solvents
- Thermodynamics of fenofibrate and solubility in pure organic solvents
- Liquid-liquid equilibrium data for ternary mixtures composed of n-hexane, benzene and acetonitrile at (298.15, 308.15, and 318.15) K
- 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
- Solid-liquid equilibrium and thermodynamic of 2,5-thiophenedicarboxylic acid in different organic solvents
- Experimental and theoretical study of interaction between organic compounds and 1- (4-sulfobutyl)-3-methylimidazolium based ionic liquids
- Isobaric vapor-liquid equilibrium of ethanenitrile + water + 1,2-ethanediol + 1-ethyl-3-methylimidazolium chloride
- Study of interaction between organic compounds and mono or dicationic oxygenated ionic liquids using gas chromatography
- Liquid liquid equilibria measurements of ternary systems (acetonitrile + a carboxylic acid + dodecane) at 303.15 K
- Solubilities of phosphoric acid, P,P0-1,4-phenylene P,P,P0,P0-tetraphenyl ester in the organic solvents
- Liquid liquid equilibria in the ternary systems {hexadecane + BTX aromatics + 2-methoxyethanol or acetonitrile} at 298.15 K
- Solid-liquid equilibrium of diphenyl anilinophosphonate in the different organic solvents
- Measurement and correlation of solubility and dissolution properties of flunixin meglumine in pure and binary solvents
- Liquid liquid and liquid liquid equilibrium for ternary system water acetonitrile cyclohexene at 298.15 K
- Thermodynamic models for determination of the solid-liquid equilibrium of oxytocin in (acetonitrile + acetone) binary solvent mixtures
- Effect of imidazolium-based ionic liquid on vapor-liquid equilibria of 2-propanol + acetonitrile binary system at 101.3 kPa
- 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
- Liquid-liquid equilibrium data for (n-hexane + ethyl acetate + acetonitrile) ternary system at (298.15, 308.15, and 318.15) K
- The isobaric vapor liquid equilibria of ethyl acetate p acetonitrile p bis(trifluoromethylsulfonyl)imide-based ionic liquids at 101.3 kPa
- Determination and correlation of solubility and solution thermodynamics of ethenzamide in different pure solvents
- Abraham model linear free energy relationships for describing the partitioning and solubility behavior of nonelectrolyte organic solutes dissolved in pyridine at 298.15 K
- Equilibrium study and diversified models of drug Norfloxacin in eight pure organic and binary solvents at T = (278.15 to 328.15) K
- In situ measurement of liquid-liquid equilibria by medium field nuclear magnetic resonance
- High selective water/butan-1-ol separation on investigation of limiting activity coefficients with [P8,8,8,8][[NTf2] ionic liquid
- Thermodynamic equilibrium of hydrocortisone form I in different solvent systems
- Separation of binary mixtures based on limiting activity coefficients data using specific ammonium-based ionic liquid and modelling of thermodynamic functions
- Solubilities of six lithium salts in five non-aqueous solvents and in a few of their binary mixtures
- Solubility and mixing thermodynamic properties of (2,4,6-trimethylbenzoyl) diphenylphosphine oxide in pure and binary solvents
- Guaiacol and its mixtures: new data and predictive models Part 2: Gibbs energy of solvation
- 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
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-butyl-1-methylpyrrolidinium dicyanamide
- Separation of acetonitrile + ethanol mixture using imidazolium - Based ionic liquids as entrainers
- New ionic liquid [P4,4,4,4][NTf2] in bio-butanol extraction on investigation of limiting activity coefficients
- Separation of acetonitrile and methanol azeotropic mixture using imidazolium-based ionic liquids as entrainers
- Ammonium ionic liquids in extraction of bio-butan-1-ol from water phase using activity coefficients at infinite dilution
- Measurements of activity coefficients at infinite dilution for organic solutes in two quaternary ammonium-based ionic liquids [DDA][ClO4] and [DDA][BF4]
- Dissolution behavior and thermodynamic properties of lapatinib ditosylate in pure and mixed organic solvents from T = (283.15-323.15) K
- Application of trihexyltetradecylphosphonium dicyanamide ionic liquid for various types of separations problems: Activity coefficients at infinite dilution measurements utilizing GLC method
- Standard partial molar volumes of some electrolytes in ethylene carbonate based mixtures
- Vapor pressures, osmotic and activity coefficients for (LiBr + acetonitrile) between the temperatures (298.15 and 343.15) K
- Experimental determination and prediction of gas solubility data for oxygen in acetonitrile
- Volumetric and compressibility behaviour of ionic liquid, 1-n-butyl-3-methylimidazolium hexafluorophosphate and tetrabutylammonium hexafluorophosphate in organic solvents at T = 298.15 K
- The (water + acetonitrile) mixture revisited: A new approach for calculating partial molar volumes
- Ultrasonic studies on binary mixtures of some aromatic ketones with acetonitrile at T = 308.15 K
- Densities and volumetric properties of (acetonitrile + an amide) binary mixtures at temperatures between 293.15 K and 318.15 K
- Application of Prigogine Flory Patterson theory to excess molar volume and speed of sound of 1-n-butyl-3-methylimidazolium hexafluorophosphate or 1-n-butyl-3-methylimidazolium tetrafluoroborate in methanol and acetonitrile
- Excess Gibbs free energies of the binary mixtures of acetonitrile with butanols at 94.83 kPa
- Isothermal compressibility and internal pressure studies of some non-electrolytes in aqueous solutions at low temperatures
- Measurement of activity coefficients at infinite dilution in 1-hexadecyl-3-methylimidazolium tetrafluoroborate ionic liquid
- (Vapor + liquid) equilibrium of the binary mixtures formed by acetonitrile with selected compounds at 95.5 kPa
- Density and speed of sound of lithium bromide with organic solvents: Measurement and correlation
- Volumetric properties of binary mixtures of ethers and acetonitrile: Experimental results and application of the Prigogine Flory Patterson theory
- Experimental study and ERAS modeling of the excess molar enthalpy of (acetonitrile + 1-heptanol or 1-octanol) mixtures at (298.15, 313.15, and 323.15) K and atmospheric pressure
- Efficient determination of crystallisation and melting points at low cooling and heating rates with novel computer controlled equipment
- Conductometric study of some alkali metal halides in (dimethyl sulfoxide + acetonitrile) at T = 298.15 K
- Heat capacities of the mixtures of ionic liquids with acetonitrile
- Volumetric properties, viscosity and refractive index of the protic ionic liquid, pyrrolidinium octanoate, in molecular solvents
- Molar heat capacities of the (water + acetonitrile) mixtures at T = (283.15, 298.15, 313.15, and 328.15) K
- Surface tension of non-ideal binary and ternary liquid mixtures at various temperatures and p = 81.5 kPa
- Volumes, heat capacities, and compressibilities of the mixtures of acetonitrile and 2-methoxyethanol
- Measurement and correlation of the excess molar enthalpy of (1-nonanol, or 1-decanol + acetonitrile) mixtures at (298.15, 303.15, and 308.15) K and atmospheric pressure
- Vapor pressures and activity coefficients of binary mixtures of 1-ethyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide with acetonitrile and tetrahydrofuran
- 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
- Excess properties of binary mixtures containing 1-hexyl-3-methylimidazolium bis(trifluoromethylsulfonyl)imide ionic liquid and polar organic compounds
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(2-methoxyethyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-hexyl-3-methylimidazolium tetracyanoborate
- Activity coefficients at infinite dilution 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
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-ethyl-3-methylimidazolium methanesulfonate
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)-1-methylpyrrolidinium bis(trifluoromethylsulfonyl)-amide
- Phase diagrams of acetonitrile or (acetone + water + EPPS) buffer phase separation systems at 298.15 K and quantum chemical modeling
- 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 solubility of Tetracycline hydrochloride in six organic solvents
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpiperidinium trifluorotris(perfluoroethyl)phosphate
- 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
- Physicochemical properties and activity coefficients at infinite dilution for organic solutes and water in a novel bicyclic guanidinium superbase-derived protic ionic liquid
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 1-(2-methoxyethyl)- 1-methylpyrrolidinium trifluorotris(perfluoroethyl)phosphate
- Measurements of activity coefficients at infinite dilution for organic solutes and water in N-hexylisoquinolinium thiocyanate, [HiQuin][SCN] using GLC
- Thermodynamic surface properties of [BMIm][NTf2] or [EMIm][NTf2] binary mixtures with tetrahydrofuran, acetonitrile or dimethylsulfoxide
- Probing subsistence of ion-pair and triple-ion of an ionic salt in liquid environments by means of conductometric contrivance
- 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
- Measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylpyrrolidinium tricyanomethanide
- (Vapour + liquid) equilibria in the ternary system (acetonitrile + n-propanol + ethylene glycol) and corresponding binary systems at 101.3 kPa
- Thermodynamics and activity coefficients at infinite dilution for organic solutes and water in the ionic liquid 1-butyl-1-methylmorpholinium tricyanomethanide
- The study of activity coefficients at infinite dilution for organic solutes and water in 1-butyl-4-methylpyridinium dicyanamide, [B4MPy][DCA] using GLC
- Measurement 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
- Physicochemical properties of two 1-alkyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide ionic liquids and of binary mixtures of 1-butyl-1-methylpyrrolidinium bis[(trifluoromethyl)sulfonyl]imide with methanol or acetonitrile
- Solution thermodynamics of iron(III)-N,N'-ethylene-bis(salicylideneiminato)-chloride in binary mixtures of N,N-dimethylformamide and acetonitrile at T = (298.15, 303.15, 308.15 and 313.15) K
- Ionic molar volumes in methanol mixtures with acetonitrile, N,N-dimethylformamide and propylene carbonate at T = 298.15 K
- 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
- Determination and correlation of cefuroxime acid solubility in (acetonitrile + water) mixtures
- Thermodynamic models for determination of the solubility of dibenzothiophene in (methanol + acetonitrile) binary solvent mixtures
- Solvation parameter model and thermodynamic parameters in a dicationic ionic liquid based on pyrrolidinium
- (Liquid + liquid) equilibrium in binary systems of isomeric C8 aliphatic monoethers with acetonitrile and its interpretation by the COSMO-SAC model
- Experimental and theoretically study of interaction between organic compounds and tricyanomethanide based ionic liquids
- Thermodynamic models for determination of the solubility of DL-malic acid in methanol plus (acetonitrile, N,N-dimethylformamide, isopropyl alcohol) binary solvent mixtures
- Solubility and solution thermodynamics of sorbic acid in eight pure organic solvents
- Activity coefficients at infinite dilution of organic solutes in methylphosphonate based ionic liquids using gas-liquid chromatography
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid 4-(3-hydroxypropyl)-4-methylmorpholinium bis(trifluoromethylsulfonyl)-amide
- 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 measurement and modelling of 1,8-dinitronaphthalene in nine organic solvents from T = (273.15 to 308.15) K and mixing properties of solutions
- Volumetric properties of binary mixtures of (acetonitrile + amines) at several temperatures with application of the ERAS model
- Solubility and solution thermodynamics of thymol in six pure organic solvents
- Solubility determination and correlation for 1,8-dinitronaphthalene in (acetone + methanol), (toluene + methanol) and (acetonitrile + methanol) mixed solvents
- Solubility modelling and thermodynamic dissolution functions of phthalimide in ten organic solvents
- Thermodynamic models for determination of the solubility of omeprazole in pure and mixture organic solvents from T = (278.15 to 333.15) K
- Solubility and solution thermodynamics of ethyl 5-amino-4-cyano-3-(2-ethoxy-2-oxoethyl)-2-thiophenecarboxylate in nine organic solvents at evaluated temperatures
- Solubility of 2,2',4,4',6,6'-hexanitrostilbene in binary solvent of N,N-dimethylformamide and acetonitrile
- 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
- Solubility measurement and thermodynamic functions of dehydroepiandrosterone acetate in different solvents at evaluated temperatures
- Experimental solubility for betulin and estrone in various solvents within the temperature range T = (293.2 to 328.2) K
- Solubility determination and thermodynamic dissolution functions of 1,3-diphenylguanidine in nine organic solvents at evaluated temperatures
- Influence of alkyl group on interactions between carboxylic acid and acetonitrile at different temperatures
- 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
- Measurement and correlation of the vapor-liquid equilibrium for methanol + acetonitrile + imidazolium-based ionic liquids at 101.3 kPa
- Solubility and solution thermodynamics of 2-methyl-6-nitroaniline in ten organic solvents at elevated temperatures
- Viscosity of binary mixtures of 1-ethyl-3-methylimidazolium tetrafluoroborate ionic liquid with four organic solvents
- 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
- Solubility determination and thermodynamic modelling of terephthaldialdehyde in ten organic solvents from T = (273.15 to 318.15) K and mixing properties of solutions
- Separation of aliphatic from aromatic hydrocarbons and sulphur compounds from fuel based on measurements of activity coefficients at infinite dilution for organic solutes and water in the ionic liquid N,N-diethyl-N-methyl-N-(2-methoxy-ethyl)ammonium bis(trifluoromethylsulfonyl)imide
- Thermodynamics and activity coefficients at infinite dilution for organic solutes in the ionic liquid 1-hexyl-2,3-dimethylimidazolium bis(trifluoromethylsulfonyl)imide
- Solubility determination and thermodynamic modeling of 3-methyl-4- nitrobenzoic acid in twelve organic solvents from T = (283.15-318.15) K and mixing properties of solutions
- Determination and correlation thermodynamic models for solid liquid equilibrium of the Nifedipine in pure and mixture organic solvents
- Measurement and modelling of econazole nitrate in twelve pure organic solvents at temperatures from 278.15 K to 318.15 K
- 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
- Determination and thermodynamic modelling for 4-nitropyrazole solubility in (methanol + water), (ethanol + water) and (acetonitrile + water) binary solvent mixtures from T = (278.15 to 318.15) K
- Densities and volumetric properties of (acetonitrile + alkyl acrylate monomer) binary mixtures at temperatures from 293.15 K to 318.15 K
- Solubility measurement and correlation of the form A of ibrutinib in organic solvents from 278.15 to 323.15 K
- Solubility determination and thermodynamic modelling of allisartan isoproxil in different binary solvent mixtures from T = (278.15 to 313.15) K and mixing properties of solutions
- Solubility of oxcarbazepine in eight solvents within the temperature range T = (288.15 308.15) K
- Thermodynamic modelling for solubility of 4-nitrobenzaldehyde in different solvents at temperature range from (273.15 to 313.15) K and mixing properties of solutions
- Determination and modelling of troxerutin solubility in eleven mono-solvents and (1,4-dioxane + 2-propanol) binary solvents at temperatures from 288.15 K to 323.15 K
- Solubility determination and thermodynamic modelling of 3-amino-1,2,4-triazole in ten organic solvents from T = 283.15 K to T = 318.15 K and mixing properties of solutions
- Solubility measurement, model evaluation and thermodynamic analysis of rivaroxaban polymorphs in organic solvents
- Solubility determination and thermodynamic modeling of paclobutrazol in nine organic solvents from T = (278.15 to 318.15) K and mixing properties of solutions
- Measurement and correlation of solubility of ciclesonide in seven pure organic solvents
- Solubility determination and correlation for o-phenylenediamine in (methanol, ethanol, acetonitrile and water) and their binary solvents from T = (283.15-318.15) K
- 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
- 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
- Experimental solubility of diosgenin and estriol in various solvents between T = (293.2-328.2) K
- 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
- Cibulka correlation for ternary excess/deviation properties of {[C2mim] [EtSO4] (x1) + acetic or propionic acid (x2) + acetonitrile (x3)} systems at different temperatures
- 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 study of solubility for pyrazinamide in ten solvents from T = (283.15 to 323.15) K
- Solubility modelling and dissolution properties of 5-phenyltetrazole in thirteen mono-solvents and liquid mixtures of (methanol + ethyl acetate) at elevated temperatures
- 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
- Thermodynamic and transport properties of acetonitrile + alkanediols liquid mixtures at different temperatures, experimental measurements and modeling
- Thermophysical approach to understand the nature of molecular interactions and structural factor between methyl isobutyl ketone and organic solvents mixtures
- Thermodynamics and activity coefficients at infinite dilution for organic compounds and water in the ionic liquid 1-butyl-3-methylimidazolium perchlorate
- Thermodynamic modelling of solubility and preferential solvation for ribavirin (II) in co-solvent mixtures of (methanol, n-propanol, acetonitrile or 1,4-dioxane) + water
- Separation of water/butan-1-ol based on activity coefficients at infinite dilution in 1,3-didecyl-2-methylimidazolium dicyanamide ionic liquid
- Separation of binary mixtures hexane/hex-1-ene, cyclohexane/cyclohexene and ethylbenzene/styrene based on gamma infinity data measurements
- Separation of binary mixtures based on gamma infinity data using [OMMIM][NTf2] ionic liquid and modelling of thermodynamic functions
- Activity coefficients at infinite dilution and physicochemical properties for organic solutes and water in the ionic liquid trihexyl-tetradecyl-phosphonium tricyanomethanide
- Thermodynamic study of molecular interaction-selectivity in separation processes based on limiting activity coefficients
- Densities, ultrasonic speeds, excess and partial molar properties of binary mixtures of acetonitrile with some alkyl methacrylates at temperatures from 293.15 K to 318.15 K
- 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]
- Thermodynamic evidence for nano-heterogeneity in solutions of the macrocycle C-butylresorcin[4]arene in non-aqueous solvents
- 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
- Solubility of dibenzothiophene in nine organic solvents: Experimental measurement and thermodynamic modelling
- Determination of the thermodynamic parameters of ionic liquid 1-propyl-3-methylimidazolium bromide by gas-liquid chromatography
- Ternary phase diagram of phenanthrene and carbazole in different solvents and its application in the separation of them
- The dissolution behavior and apparent thermodynamic analysis of temozolomide in pure and mixed solvents
- Solubility 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
- Separation of (water/butan-1-ol) binary systems based on activity coefficients at infinite dilution with phosphonium ionic liquid
- The dissolution behaviour and apparent thermodynamic analysis of diprophylline in pure and mixed solvents
- Co-solvence phenomenon and thermodynamic properties of edaravone in pure and mixed solvents
- Solvent effect on solubility and preferential solvation analysis of buprofezin dissolved in aqueous co-solvent mixtures of N,N-dimethylformamide, ethanol, acetonitrile and isopropanol
- Thermodynamic properties of ternary mixture {[C4mim][SCN] + acetic or propionic acid + acetonitrile} over the temperature range of (293.15-313.15) K
- Measurement and correlation of isobaric vapour-liquid equilibrium for the (acetonitrile + water) system containing different ionic liquids at atmospheric pressure
- ERAS modeling of the excess molar enthalpies of binary liquid mixtures of 1-pentanol and 1-hexanol with acetonitrile at atmospheric pressure and 288, 298, 313 and 323K
- Densities, viscosities, excess molar volumes, and refractive indices of acetonitrile and 2-alkanols binary mixtures at different temperatures: Experimental results and application of the Prigogine Flory Patterson theory
- Molecular interaction studies and theoretical estimation of ultrasonic speeds using scaled particle theory in binary mixtures of toluene with homologous nitriles at different temperatures
- EXCESS MOLAR ENTHALPIES OF DIBROMOMETHANE WITH ACETONITRILE,FURAN AND ACETOPHENONE 303.15 K
- Solubilities of succinimide in different pure solvents and binary methanol+ethyl acetate solvent mixtures
- Physics and Chemistry of Lithium Halides in 1,3-Dioxolane and Its Binary Mixtures with Acetonitrile probed by Conductometric, Volumetric, Viscometric, Refractometric and Acoustic Study
- Probing molecular interactions of ionic liquid in industrially important solvents by means of conductometric and spectroscopic approach
- Solubilities of Phosphoramidic Acid, N-(phenylmethyl)-, Diphenyl Ester in Selected Solvents
- Solubility of 3,7-Dinitro-1,3,5,7-tetraazabicyclo [3.3.1] Nonane in Ethanenitrile, Methanol, 1,1-Dichloroethane, Dimethyl Sulfoxide, Acetone, and Mixed Solvents
- Solubility and Caloric Properties of Cinnarizine
- Solubility and Saturation Apparent Volume of Propranolol Hydrochloride in Some Binary Aqueous Cosolvent Mixtures at 298.15 K
- Phase Equilibria in Systems of Morpholine, Acetonitrile, and n-Alkanes
- Solubility and Solution Thermodynamics of Gibberellin A4 in Different Organic Solvents from 278.15 K to 333.15 K
- Solid Forms, Crystal Habits, and Solubility of Danthron
- Solubilities of 3-Chlorophthalic Anhydride and 4-Chlorophthalic Anhydride in Different Pure Solvents
- Solubility of Trimethoprim in Selected Pure Solvents and (Water + Ethanol/2-Propanol) Mixed-Solvent Systems
- Exploration of Solvation Consequence of Ionic Liquid [Bu4PCH3SO3] in Various Solvent Systems by Conductance and FTIR Study
- 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
- Vapor Liquid Equilibria Measurement of (Methanol + Ethanenitrile + Bis(trifluoromethylsulfonyl) Imide)-Based Ionic Liquids at 101.3 kPa
- Excess Enthalpies in Binary Systems of Isomeric C8 Aliphatic Monoethers with Acetonitrile and Their Description by the COSMO-SAC Model
- Activity Coefficients at Infinite Dilution of Organic Solutes and Water in Tributylethylphosphonium Diethylphosphate Using Gas Liquid Chromatography: Thermodynamic Properties of Mixtures Containing Ionic Liquids
- Isobaric Vapor Liquid Equilibria for Ethyl Acetate + Acetonitrile + 1-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide at 101.3 kPa
- Solubility Modeling of 4-(Methylsulfonyl)benzaldehyde in Nine Organic Solvents at Elevated Temperatures
- 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
- 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 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
- 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 Three Flavonoids in Different Natural Deep Eutectic Solvents at T = (288.15 to 328.15) 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
- 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
- Determination and Thermodynamic Modeling of Solid Liquid Phase Equilibrium for Esomeprazole Sodium in Monosolvents and in the (Ethanol + Ethyl Acetate) Binary Solvent Mixtures
- Phase Behavior of Binary Mixtures Containing Succinic Acid or Its Esters
- Measurement and Correlation of Solubility of Theobromine, Theophylline, and Caffeine in Water and Organic Solvents at Various Temperatures
- Experimental Measurement and Modeling of Vapor Liquid Equilibrium for the Ternary System Water + Acetonitrile + Ethylene Glycol
- Solid Liquid Phase Equilibrium of N,N'-Piperazinebis(neopentylglycol)phosphoramidate in Selected Solvents from T = (293.15 to 333.15) 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
- Excess Molar Volumes, Excess Molar Isentropic Compressibilities, Viscosity Deviations, and Activation Parameters for 1-Ethyl-3-methyl-imidazolium Trifluoro-methanesulfonate + Dimethyl Sulfoxide and/or Acetonitrile at T = 298.15 to 323.15 K and P = 0.1 MPa
- Solid-Liquid Phase Equilibrium and Thermodynamic Properties of Olaparib in Selected Organic Solvents and (Tetrahydrofuran + MTBE, Acetonitrile + Isopropyl Alcohol) Binary Solvent Mixtures
- 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
- Thermodynamic Functions for the Solubility of 3-Nitrobenzonitrile in 12 Organic Solvents from T/K = (278.15 to 318.15)
- Measurement and Correlation of Solubility of Resorcinol Bis(cyclic 2,2-dimethyl-1,3-propanediol phosphate) in Selected Solvents from T = 293.15 to 333.15 K
- Solubility 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
- Pressure-Drop Method for Detecting Bubble and Dew Points of Multicomponent Mixtures at Temperatures of up to 573 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
- Density, Electrical Conductivity, Dynamic Viscosity, Excess Properties, and Molecular Interactions of Ionic Liquid 1-Cyanopropyl-3-methylimidazolium Tetrafluoroborate and Binary System with Acetonitrile
- Solubility of 2,5-Furandicarboxylic Acid in Eight Pure Solvents and Two Binary Solvent Systems at 313.15-363.15 K
- The Thermodynamic and Excess Properties of Trialkyl-Substituted Imidazolium-Based Ionic Liquids with Thiocyanate and Its Binary Systems with Acetonitrile
- Solubility Measurement and Thermodynamic Modeling of N-(4-Methylphenyl-Z-3-chloro-2-(phenylthio)propenamide in 12 Pure Solvents at Temperatures Ranging from 278.15 to 318.15 K
- Solution Thermodynamics of Benzotriazole in Different Pure Solvents
- Solubility of Ionic Liquid [Bmim]Ac in Supercritical CO2 Containing Different Cosolvents
- Solubility of Sulfachloropyridazine in Pure and Binary Solvent Mixtures and Investigation of Intermolecular Interactions
- Determination of Activity Coefficients at Infinite Dilution of Organic Solutes in the Ionic Liquid 1-(2-Hydroxyethyl)-3-methylimidazolium Nonafluoro-1-butanesulfonate Using Gas-Liquid Chromatography
- Liquid-Liquid Equilibrium for Ternary Systems, Water + 5-Hydroxymethylfurfural + (1-Butanol, Isobutanol, Methyl Isobutyl Ketone), at 313.15, 323.15, and 333.15 K
- 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
- Effect of Solvents and Temperature on Interactions in Binary and Ternary Mixtures of 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate with Acetonitrile or/and N,N-Dimethylformamide
- 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
- Acetonitrile Dehydration via Extractive Distillation Using Low Transition Temperature Mixtures as Entrainers
- Solubility and Molecular Interactions of Trimetazidine Hydrochloride in 12 Monosolvents and Solvent Mixtures of Methanol + (Ethanol, N,N-Dimethylformamide or Ethyl Acetate)
- Solubility Measurement, Modeling, and Thermodynamic Functions for para-Methoxyphenylacetic Acid in Pure and Mixed Organic and Aqueous Systems
- Research on Dissolution Capability of Several Antofloxacin Salts
- 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
- Measurement and Correlation of the Solubility of 5-Fluorouracil in Pure and Binary Solvents
- Solubility Modeling and Solvent Effects of Allopurinol in 15 Neat Solvents
- Solubilities of Organic Semiconductors and Nonsteroidal Anti-inflammatory Drugs in Pure and Mixed Organic Solvents: Measurement and Modeling with Hansen Solubility Parameter
- Thermodynamic Study of Solubility for Imatinib Mesylate in Nine Monosolvents and Two Binary Solvent Mixtures from 278.15 to 318.15 K
- Solubility Measurements at 296 and 310 K and Physicochemical Characterization of Abiraterone and Abiraterone Acetate
- Thermodynamic Parameters of a New Synthesized Tricationic Ionic Liquid Stationary Phase by Inverse Gas Chromatography
- Determination of Activity Coefficients at Infinite Dilution of Solutes in N,N'-Di(2-ethylhexyl)isobutyramide Using Inverse Gas-Liquid Chromatography
- Viscosities of 1-Hexyl-3-methylimidazolium Tetrafluoroborate and Its Binary Mixtures with Dimethyl Sulfoxide and Acetonitrile
- 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
- Solid-Liquid Equilibrium of Rebaudioside A in Pure and Binary Mixed Solvents at T = (288.15 to 328.15) K
- Solubility and Data Correlation of Isoniazid in Different Pure and Binary Mixed Solvent Systems from 283.15 K to 323.15 K
- Measurement and Correlation of the Solubility of Tetramethylpyrazine in Nine Monosolvents and Two Binary Solvent Systems
- Measurement and Correlation of Solubility of Gatifloxacin in 12 Pure Solvents from 273.15 K to 318.15 K
- Solubility Measurement and Thermodynamic Model Correlation and Evaluation of 2-Chloro-5-nitroaniline in 12 Pure Solvents
- Experimental Solubility and Density Functional Theory Studies of Deferasirox in Binary Solvent Mixtures: Performance of Polarizable Continuum Model and Jouyban-Acree Model
- Equilibrium Solubility of Biapenem in Different Neat and Binary Solvents: Experimental Determination and Model Correlation
- Effect of Solvent Properties and Composition on the Solubility of Ganciclovir Form I
- Measurement and Modeling of Solid-Liquid Equilibria of l-Glutamic Acid in Pure Solvents and Aqueous Binary Mixtures
- 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
- 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
- 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 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
- Isobaric Vapor-Liquid Equilibrium of the Acetonitrile + 1-Propanol + Ionic Liquids at an Atmospheric Pressure
- Solid-Liquid Equilibrium of 5-Chloro-8-hydroxyquinoline and 5,7-Dichloro-8-hydroxyquinoline in Different Solvents and Mixing Properties of Solutions
- 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
- 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
- Solubility and Solution Thermodynamics of Flufenamic Acid Polymorphs in Two Binary Solvents
- Solubility of Gastrodin in Pure and Mixed Solvents at 273.15-313.15 K and Its Correlation with Different Thermodynamic Models
- Solubility Measurement and Correlation of 2-Oxindole in 12 Pure Organic Solvents
- Effect of Cosolvents on the Solubility of Lenalidomide and Thermodynamic Model Correlation of Data
- Assessment of Pyrrolidinium-Based Ionic Liquid for the Separation of Binary Mixtures Based on Activity Coefficients at Infinite Dilution
- Solubility Measurement and Phase Equilibrium Modeling of 2-Aminobenzamide in 15 Pure Solvents
- Measurement of the Solubility of Diclazuril and Discussion of the Effect of the Cosolvent
- Solubility Determination, Modeling, and Thermodynamic Dissolution Properties of Benzenesulfonamide in 16 Neat Solvents from 273.15 to 324.45 K
- 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, 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
- Acetonitrile and Na+ or K+ Salts as Constituents of the Aqueous Two-Phase System: Equilibrium Data and Capsaicin Purification
- Solubility and Solvent Effect of 1-(2-Bromo-phenyl)-pyrrole-2,5-dione in 14 Pure Solvents from 278.15 to 323.15 K
- Saturated Solubility and Thermodynamic Evaluation of l-Tryptophan in Eight Pure Solvents and Three Groups of Binary Mixed Solvents by the Gravimetric Method at T = 278.15-333.15 K
- Solubility Measurement and Modeling of 3-Hydroxy-2-nitropyridine in Ten Pure Solvents and Two Binary Mixed Solvents for T = (278.15-318.15) K
- Solubility 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
- 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 Increment and Thermodynamic Analysis of Bioactive Antofloxacin Hydrochloride in Aqueous ChCl/PTS Deep Eutectic Solvent and Cosolvent Mixtures
- Solubility and Solution Thermodynamics of 2,6-Dichloro-4-nitroaniline in 12 Pure Solvents at Temperatures from 278.15 to 323.15 K
- Solubility Behavior and Data Modeling of l-Proline in Different Neat and Binary Solvent Systems
- 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
- Vapor-Liquid Equilibria for Four Binary Systems at 363.15 K: N-Methylformamide + Hexane, + Benzene, + Chlorobenzene, and + Acetonitrile
- High Pressure Phase Equilibria of the Related Substances in the Limonene Oxidation in Supercritical CO2
- Solubility of Anthracene in Binary Alcohol + Acetonitrile Solvent Mixtures at 298.2 K
- Solubility in Binary Solvent Mixtures: Anthracene Dissolved in Alcohol + Acetonitrile Mixtures at 298.2 K
- Solubility in Binary Solvent Mixtures: Pyrene Dissolved in Alcohol + Acetonitrile Mixtures at 299.2 K
- Vapor-Liquid Equilibrium for Acetonitrile + Propanenitrile and 1-Pentanamine + 1-Methoxy-2-propanol
- Isothermal Vapor-Liquid Equilibrium Data for the Systems 1,4-Dioxane + Water + Tetrabutylammonium Nitrate and Acetonitrile + Water + Tetrabutylammonium Bromide
- Vapor Pressures of Acetonitrile Determined by Comparative Ebulliometry
- Effect of Organic Cosolvents on the Solubility of Ionic Liquids in Supercritical CO2
- Thermodynamic Properties of Inorganic Salts in Nonaqueous Solvents. II. Apparent Molar Volumes and Compressibilities of Divalent Transition-Metal Perchlorates in Acetonitrile
- High-Pressure Vapor-Liquid Equilbria of Some Carbon Dioxide + Organic Binary Systems
- Liquid Thermal Conductivities of Acetonitrile, Diethyl Sulfide, Hexamethyleneimine, Tetrahydrothiophene, and Tetramethylethylenediamine
- Liquid-Liquid Equilibrium for the Water + Acetonitrile + Limonene System at different temperatures
- Volumetric and Speed of Sound of Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate with Acetonitrile and Methanol at T ) (298.15 to 318.15) K
- Experimental (Solid + Liquid) and (Liquid + Liquid) Equilibria and Excess Molar Volume of Alkanol + Acetonitrile, Propanenitrile, and Butanenitrile Mixtures
- Vapor-Liquid Equilibria on Seven Binary Systems: Ethylene Oxide + 2-Methylpropane; Acetophenone + Phenol; cis-1,3-Dichloropropene + 1,2-Dichloropropane; 1,5-Hexadiene + Allyl Chloride; Isopropyl Acetate + Acetonitrile; Vinyl Chloride + Methyl Chloride; and 1,4-Butanediol + c-Butyrolactone
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 8. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in 1-Hexyl-3-methylimidazolium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography
- Thermodynamic Properties of Mixtures Containing Ionic Liquids. 9. Activity Coefficients at Infinite Dilution of Hydrocarbons, Alcohols, Esters, and Aldehydes in Trimethyl-butylammonium Bis(trifluoromethylsulfonyl) Imide Using Gas-Liquid Chromatography and Static Method
- Density and Surface Tension of Binary Mixtures of Acetonitrile + 1-Alkanol at 293.15 K
- Vapor-Liquid Equilibrium Data for the Binary Methyl Esters (Butyrate, Pentanoate, and Hexanoate) (1) + Acetonitrile (2) Systems at 93.32 kPa
- Thermodynamic Properties of Mixtures Containing Ionic Liquids: Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Propyl Boronic Acid-3-Alkylimidazolium Bromide and 1-Propenyl-3-alkylimidazolium Bromide Using Inverse Gas Chromatography
- Measurement and Correlation of Isothermal Vapor-Liquid Equilibrium Data for the System Acetonitrile + Water + Tetrapropylammonium Bromide
- Compressibility Studies of Binary Solutions Involving Water as a Solute in Nonaqueous Solvents at T ) 298.15 K
- Solubility and Melting Properties of Salicylic Acid
- Solubilities of Some Phosphaspirocyclic Compounds in Selected Solvents
- Solubility and Melting Properties of Salicylamide
- Experimental Study of Thermodynamic Properties of Mixtures Containing Ionic Liquid 1-Ethyl-3-methylimidazolium Ethyl Sulfate Using Gas-Liquid Chromatography and Transpiration Method
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Studies on Thermodynamic and Transport Properties of Binary Mixtures of Acetonitrile with Some Cyclic Ethers at Different Temperatures by Volumetric, Viscometric, and Interferometric Techniques
- Vapor-Liquid Equilibria for the Ternary System Acetonitrile + 1-Propanol + Dimethyl Sulfoxide and the Corresponding Binary Systems at 101.3 kPa
- Solubility of Artemisinin in Different Single and Binary Solvent Mixtures Between (284.15 and 323.15) K and NRTL Interaction Parameters
- Experimental Data and Correlation of Surface Tensions of the Binary and Ternary Systems of Water + Acetonitrile + 2-Propanol at 298.15 K and Atmospheric Pressure
- Densities and Excess Molar Volumes for Binary Mixtures of Ionic Liquid 1-Ethyl-3-methylimidazolium Ethylsulfate with Solvents
- Phase Separation Conditions for Sugaring-Out in Acetonitrile-Water Systems
- Volumetric Properties of Binary Mixtures Containing Ionic Liquids and Some Aprotic Solvents
- Solubilities of Phosphorus-Containing Compounds in Selected Solvents
- Calorimetric Study of Nitrile Group-Solvent Interactions and Comparison with Dispersive Quasi-Chemical (DISQUAC) Predictions
- Volumes, Heat Capacities, and Compressibilities of the Mixtures of Acetonitrile with N,N-Dimethylacetamide and Propylene Carbonate
- Activity Coefficients at Infinite Dilution for Hydrocarbons in Fatty Alcohols Determined by Gas-Liquid Chromatography
- Solubility of Butyl Paraben in Methanol, Ethanol, Propanol, Ethyl Acetate, Acetone, and Acetonitrile
- Volumetric Properties, Viscosities, and Isobaric Heat Capacities of Imidazolium Octanoate Protic Ionic Liquid in Molecular Solvents
- Viscosities of Acetate or Chloride-Based Ionic Liquids and Some of Their Mixtures with Water or Other Common Solvents
- Solubilities of N-[(4-Bromo-3,5-difluorine)-phenyl]maleimide in Pyridine, Acetone, Tetrahydrofuran, Ethanol, Trichloromethane, and Acetonitrile at Temperature between (285.00 and 350.15) K
- Solubilities of (a,Z)-2-Amino-a-(methoxyimino)-4-thiazoleethanethioic Acid S-2-Benzothiazolyl Ester in Different Pure Solvents and Binary Mixtures of Tetrahydrofuran + Dichloromethane or 1,2-Dichloroethane
- Solubilities of Phenylphosphinic Acid, Methylphenylphosphinic Acid, Hexachlorocyclotriphosphazene, and Hexaphenoxycyclotriphosphazene in Selected Solvents
- Solubility of Candesartan Cilexetil in Different Solvents at Various Temperatures
- 1-Ethyl-3-methylimidazolium Ethylsulfate in Water, Acetonitrile, and Dichloromethane: Molar Conductivities and Association Constants
- Surface Tensions and the Gibbs Excess Surface Concentration of Binary Mixtures of the Ionic Liquid 1-Ethyl-3-methylimidazolium Bis[(trifluoromethyl)sulfonyl]imide with Tetrahydrofuran and Acetonitrile
- Physico-Chemical Properties of Non-Newtonian Shear Thickening Diisopropyl-ethylammonium-Based Protic Ionic Liquids and Their Mixtures with Water and Acetonitrile
- Measurement and Correlation for the Solubility of Dimethyl 1,4-Cyclohexanedione-2,5-dicarboxylate in Different Solvents at Temperatures from (278.15 to 323.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Butyl-3-methylimidazolium Nitrate Using Gas-Liquid Chromatography
- Solubility of 2-(2,4,6-Trichlorophenoxy)ethyl Bromide in Methanol, Ethanol, Propanol, Isopropanol, Acetonitrile, n-Heptane, and Acetone
- Solubility of Urea in Acetonitrile Water Mixtures and Liquid Liquid Phase Separation of Urea-Saturated Acetonitrile Water Mixtures
- Activity Coefficients at Infinite Dilution of Organic Compounds in Four New Imidazolium-Based Ionic Liquids
- Solubilities of Tris(o-phenylenedioxy)cyclotriphosphazene in Selected Solvents
- Electrical Conductivity of Solutions of Ionic Liquids with Methanol, Ethanol, Acetonitrile, and Propylene Carbonate
- Partition Coefficients of Organic Compounds in Four New Tetraalkylammonium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Using Inverse Gas Chromatography
- Interactions of Volatile Organic Compounds with the Ionic Liquid 1-Butyl-1-methylpyrrolidinium Dicyanamide
- Evaluation of the Performance of Trigeminal Tricationic Ionic Liquids for Separation Problems
- Volumetric Properties of Binary Mixtures of Two 1-Alkyl-3-Methylimidazolium Tetrafluoroborate Ionic Liquids with Molecular Solvents
- Electrical Conductances of 1-Butyl-3-propylimidazolium Bromide and 1-Butyl-3-propylbenzimidazolium Bromide in Water, Methanol, and Acetonitrile at (308, 313, and 318) K at 0.1 MPa
- 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
- Crystal Structures, Reaction Rates, and Selected Physical Properties of Halo-Boronsubphthalocyanines (Halo = Fluoride, Chloride, and Bromide)
- Activity Coefficients at Infinite Dilution for Organic Compounds Dissolved in 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Having Six-, Eight-, and Ten-Carbon Alkyl Chains
- Properties of Pure 1-Butyl-2,3-dimethylimidazolium Tetrafluoroborate Ionic Liquid and Its Binary Mixtures with Dimethyl Sulfoxide and Acetonitrile
- Isobaric Vapor Liquid Equilibrium for the Acetonitrile + Water System Containing Different Ionic Liquids at Atmospheric Pressure
- Determination of Henry's Law Constants Using Internal Standards with Benchmark Values
- 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
- Vapor Liquid Equilibrium, Excess Molar Enthalpies, and Excess Molar Volumes of Binary Mixtures Containing 2-Ethoxy-2-methylpropane or 2-Ethoxy-2-methylbutane and Acetonitrile or Propanenitrile
- Activity Coefficients at Infinite Dilution for Organic Solutes Dissolved in Three 1-Alkyl-1-methylpyrrolidinium Bis(trifluoromethylsulfonyl)imide Ionic Liquids Bearing Short Linear Alkyl Side Chains of Three to Five Carbons
- 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
- Apparent Molar Volumes of 1-Alkyl (n = 2, 4, 6)-3-methylimidazolium Bromides in a Mixed-Solvent Medium of Acetonitrile + Water at Temperatures of (293.15, 303.15, and 313.15) K
- Isobaric Vapor Liquid Equilibrium for the Extractive Distillation of Acetonitrile + Water Mixtures Using Dimethyl Sulfoxide at 101.3 kPa
- Solubility of Sodium Acetate in Binary Mixtures of Methanol, 1-Propanol, Acetonitrile, and Water at 298.2 K
- Acoustic and Volumetric Properties of Binary Mixtures of Ionic Liquid 1-Butyl-3-methylimidazolium Bis(trifluoromethylsulfonyl)imide with Acetonitrile and Tetrahydrofuran
- Apparent Molar Volumes and Expansivities of Ionic Liquids Based on N-Alkyl-N-methylmorpholinium Cations in Acetonitrile
- Solubilities of 4-(Hydroxymethyl)-1-oxido-2,6,7-trioxa-1-phosphabicyclo[2.2.2]octane in Organic Solvents
- Liquid Liquid Equilibria for the Ternary Systems of 4-Methyl-1,3-dioxolan-2-one + 1,4-Dimethylbenzene + Octane, Decane, or Dodecane and the Ternary Systems of Acetonitrile + Morpholine + Octane, Decane, or Dodecane at 313.15 K or 298.15 K
- Solid Liquid Phase Equilibria of N,N'-[1,3-Phenylenebis(methylene)]bis(phosphoramidic acid) P,P,P',P'-Tetraphenyl Ester in 10 Pure Solvents
- Infinite Dilution Activity Coefficients of Solutes Dissolved in Two Trihexyl(tetradecyl)phosphonium Ionic Liquids
- Determination and Correlation of Solubilities of Lithium Bis(oxalate)borate in Six Different Solvents from (293.15 to 363.15) K
- 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
- Measurement and Correlation of the Solubility of Enrofloxacin in Different Solvents from (303.15 to 321.05) 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
- Thermodynamic Models for Determination of the Solubility of Dibenzothiophene in Different Solvents at Temperatures from (278.15 to 328.15) K
- Ternary Liquid Liquid Equilibrium Data for the Water + Acetonitrile + {Butan-1-ol or 2-Methylpropan-1-ol} Systems at (303.2, 323.2, 343.2) K and 1 atm
- 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
- Density, Viscosity, Speed of Sound, and Refractive Index of a Ternary Solution of Aspirin, 1-Butyl-3-methylimidazolium Bromide, and Acetonitrile at Different Temperatures T = (288.15 to 318.15) K
- Thermodynamic Models for Determination of the Solubility of Sulfanilic Acid in Different Solvents at Temperatures from (278.15 to 328.15) K
- Thermodynamic Models for Determination of the Solubility of the (1:1) Complex of (Urea + l-Malic Acid) in (Methanol + Acetonitrile) Binary Solvent Mixtures
- Solubility and Solution Thermodynamics of Diphenoxylate in Different Pure Solvents
- Solubility of 3,3'-(Oxidi-2,1-ethanediyl)bis[1-methyl-imidazolium] Dihexafluorophosphate in Water, Methanol, Ethanol, Acetone, and Acetonitrile and Binary Mixtures (Water + DMF) from (283.00 to 323.00) K
- Densities and Viscosities of Ternary N,N'-Bis(2-pyridylmethylidene)-1,2-diiminoethane Schiff Base + Imidazolium Based Ionic Liquids + Acetonitrile Solutions at T = (298.15 to 313.15) K
- Solid Liquid Phase Equilibrium of Phosphoramidic acid, N,N'-1,2-Ethanediylbis-P,P,P',P'-tetraphenyl Ester in Selected Solvents
- Viscosity, Density, and Speed of Sound for the Binary Mixtures of Formamide with 2-Methoxyethanol, Acetophenone, Acetonitrile, 1,2-Dimethoxyethane, and Dimethylsulfoxide at Different Temperatures
- Solubility of Flavonoids in Organic Solvents
- Thermodynamic Properties of Inorganic Salts in Nonaqeous Solvents. IV. Apparent Molar Volumes and Compressibilities of Divalent Transition-Metal Bromides and Chlorides in Acetonitrile
- Solid-Liquid Equilibria of Dibenzothiophene and Dibenzothiophene Sulfone in Organic Solvents
- Densities of Ionic Liquids, 1-Butyl-3-methylimidazolium Hexafluorophosphate and 1-Butyl-3-methylimidazolium Tetrafluoroborate, with Benzene, Acetonitrile, and 1-Propanol at T = (293.15 to 343.15) K
- Viscosity, Density, Speed of Sound, and Refractive Index of Binary Mixtures of Organic Solvent + Ionic Liquid, 1-Butyl-3-methylimidazolium Hexafluorophosphate at 298.15 K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Butyl-3-methylimidazolium Trifluoromethanesulfonate Using Gas Liquid Chromatography
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-Propyl-2,3-dimethylimidazolium Tetrafluoroborate Using Gas Liquid Chromatography
- Densities and Volumetric Properties of Binary and Ternary Liquid Mixtures of Water (1) + Acetonitrile (2) + Dimethyl Sulfoxide (3) at Temperatures from (293.15 to 333.15) K and at Ambient Pressure (81.5 kPa)
- solubility of L-(+)-ascorbic acid in water, ethanol, methanol, propan-2-ol, acetone, acetonitrile, ethyl acetate, and tetrahydrofuran from (293 to 323) K
- Density and Viscosity of Anhydrous Mixtures of Dimethylsulfoxide with Acetonitrile in the Range (298.15 to 318.15) K
- Activity Coefficients at Infinite Dilution of Organic Solutes in 1-Ethyl-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Thermodynamic Study of Phenyl Salicylate Solutions in Aprotic Solvents at Different Temperatures
- Ternary Liquid-Liquid Equilibria of Acetonitrile and Water with Heptanoic Acid and Nonanol at 323.15 K and 1 atm
- Conductivities of Binary Mixtures of Ionic Liquids with Polar Solvents
- Solubility of Artemisinin in Seven Different Pure Solvents from (283.15 to 323.15) K
- Isothermal Vapor-Liquid Equilibrium of Binary Mixtures Containing 1-Chlorobutane, Ethanol, or Acetonitrile
- Vapor Pressures for the Acetonitrile + Tetrabutylammonium Bromide, Water + Tetrabutylammonium Bromide, and Acetonitrile + Water + Tetrabutylammonium Bromide Systems
- Solubility of Desmosterol in Five Organic Solvents
- Activity Coefficients at Infinite Dilution of Organic Compounds in 1-Butyl-3-methylimidazolium Tetrafluoroborate Using Inverse Gas Chromatography
- Solubility of Chloroquine Diphosphate and 4,7-Dichloroquinoline in Water, Ethanol, Tetrahydrofuran, Acetonitrile, and Acetone from (298.2 to 333.2) K
- Activity Coefficients at Infinite Dilution of Organic Compounds in Trihexyl(tetradecyl)phosphonium Bis(trifluoromethylsulfonyl)imide Using Inverse Gas Chromatography
- Solubility of Valsartan in Different Organic Solvents and Ethanol + Water Binary Mixtures from (278.15 to 313.15) K
- Diffusion Coefficients of 1-Alkyl-3-methylimidazolium Ionic Liquids in Water, Methanol, and Acetonitrile at Infinite Dilution
- Solubility of Tiamulin Hydrogen Fumarate in Acetone, Acetonitrile, Ethyl Acetate, Ethyl Formate, and Butyl Acetate from (288.2 to 318.2) K
- Densities of Ionic Liquid [BMIM][BF4] + Ethanol, + Benzene, and + Acetonitrile at Different Temperature and Pressure
- Solubility of Thiotriazinone in Ethanol, 1-Propanol, 2-Propanol, 1-Butanol, Acetonitrile, Acetone, Ethyl Acetate, and Water from 293 K to 343 K
- Partition Coefficients of Organic Compounds in New Imidazolium and Tetralkylammonium Based Ionic Liquids Using Inverse Gas Chromatography
- Solubility of Captopril in 2-Propanol, Acetone, Acetonitrile, Methyl Acetate, Ethyl Acetate, and Butyl Acetate
- Partial Molar Volumes of Butyltriethylammonium Iodide in Single Nonaqueous Solvents at 298.15 K
- Solubility of Camellianin A in Methanol, Acetonitrile, Acetone, and Water from (283.2 to 313.2) K
- Solubilities of N-[(4-Bromo-3,5-difluorine)phenyl]acrylamide in Benzene, Methanol, Pyridine, Ethanol, Acetonitrile, and Toluene at Temperatures between (284.65 and 348.95) K
- Activity Coefficients at Infinite Dilution of Polar Solutes in 1-(2-Hydroxyethyl)-3-methylimidazolium Tetrafluoroborate Using Gas-Liquid Chromatography
- Volumetric Properties of Binary Mixtures of 1-Butyl-3-methylimidazolium Chloride + Water or Hydrophilic Solvents at Different Temperatures
- Solubilities of (?,Z)-2-Amino-?-(methoxyimino)-4-thiazole-ethanethioic Acid S-2-Benzothiazolyl Ester in Pure Solvents and a Mixture of Acetonitrile and Dichloromethane
- Study of Ether-, Alcohol-, or Cyano-Functionalized Ionic Liquids Using Inverse Gas Chromatography
- Apparent Molar Volume and Compressibility of Tetrabutylphosphonium Bromide in Various Solvents
- Compressibility Studies of Some Copper(I), Silver(I), and Tetrabutylammonium Salts in Acetonitrile + Adiponitrile Binary Mixtures
- Solubility of Triadimefon in Organic Solvents at Temperatures between (288.15 and 333.15) K
- Joback Method
- KDB
- Aqueous Solubility Prediction Method
- Estimated Solubility Method
- McGowan Method
- NIST Webbook
- The Yaws Handbook of Vapor Pressure
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