43 results on '"Hofman, Tadeusz"'
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2. The phase split forced by salts or carbohydrates in nonaqueous systems
3. Problems and Limitations in the Calculation of Liquid-Liquid Equilibrium
4. Solid-liquid equilibria in systems consisting of potassium pseudohalides and amides
5. The Phase Split Forced by Salts or Carbohydrates in Nonaqueous Systems
6. Equilibria in the 3-(trifluoromethyl)phenylboronic acid - boroxine system. Solubility of the acid and its cyclic esters in organic solvents
7. Solid-liquid equilibria and excess enthalpies in binary mixtures of propiophenone with some aliphatic amides
8. Equilibrium Solubility Determination and Correlation of Isobutoxyphenylboronic Acids in Organic Solvents
9. Solubility of Phenylboronic Acid and its Cyclic Esters in Organic Solvents
10. Solid-liquid equilibria and excess enthalpies in binary mixtures of acetophenone with some aliphatic amides
11. The influence of bromide-based ionic liquids on solubility of {LiBr (1) + water (2)} system. Experimental (solid + liquid) phase equilibrium data. Part 1
12. Excess Enthalpies in Binary Systems of Isomeric C8 Aliphatic Monoethers with Acetonitrile and Their Description by the COSMO-SAC Model
13. (Liquid + liquid) equilibrium in binary systems of isomeric C8 aliphatic monoethers with acetonitrile and its interpretation by the COSMO-SAC model
14. Liquid–liquid equilibrium in binary systems of isomeric C8 aliphatic monoethers with nitromethane
15. Corrigendum to “Volumetric properties of ternary (IL + 2-propanol or 1-butanol or 2-butanol + ethyl acetate) systems and binary (IL + 2-propanol or 1-butanol or 2-butanol) and (1-butanol or 2-butanol + ethyl acetate) systems” [J. Chem. Thermodyn. 49 (2012) 24–38]
16. Volumetric Properties of the {x 1[C4mim][MeSO4] + (1 − x 1)MeOH} System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
17. Volumetric properties of the ionic liquids: [C6mim][MeSO4], [C6mim][EtSO4], [C4mim][EtSO4] and their mixtures with methanol or ethanol
18. Heat capacities and excess enthalpies of the (N-hexylisoquinolinium thiocyanate ionic liquid + water) binary systems
19. Vapor–Liquid Equilibrium Data for Binary Systems of 1-Methyl-4-(1-methylethenyl)-cyclohexene + {Ethanol, Propan-1-ol, Propan-2-ol, Butan-1-ol, Pentan-1-ol, or Hexan-1-ol} at 40 kPa
20. Volumetric properties of ternary (IL + 2-propanol or 1-butanol or 2-butanol + ethyl acetate) systems and binary (IL + 2-propanol or 1-butanol or 2-butanol) and (1-butanol or 2-butanol + ethyl acetate) systems
21. Densities, isobaric expansivities and isothermal compressibilities of the thiocyanate-based ionic liquids at temperatures (298.15–338.15K) and pressures up to 10MPa
22. High-pressure volumetric properties of ionic liquids: 1-butyl-3-methylimidazolium tetrafluoroborate, [C4mim][BF4], 1-butyl-3-methylimidazolium methylsulfate [C4mim][MeSO4] and 1-ethyl-3-methylimidazolium ethylsulfate, [C2mim][EtSO4]
23. Volumetric Properties for (Ionic Liquid + Methanol or Ethanol or 1-Propanol + Nitromethane) at 298.15 K and Atmospheric Pressure
24. The phase envelopes of alternative solvents (ionic liquid, CO2) and building blocks of biomass origin (lactic acid, propionic acid)
25. Isothermal vapour–liquid equilibria in the binary and ternary systems consisting of an ionic liquid, 1-propanol and CO2
26. Densities, Excess Volumes, Isobaric Expansivities, and Isothermal Compressibilities of the 1-Ethyl-3-methylimidazolium Ethylsulfate + Ethanol System at Temperatures (283.15 to 343.15) K and Pressures from (0.1 to 35) MPa
27. Preface
28. Densities, excess volumes, isobaric expansivity, and isothermal compressibility of the (1-ethyl-3-methylimidazolium ethylsulfate + methanol) system at temperatures (283.15 to 333.15) K and pressures from (0.1 to 35) MPa
29. Densities and Excess Volumes of the 1-Chlorobutane + n-Hexane System at Temperatures from (283.15 to 333.15) K and Pressures from (0.1 to 35) MPa
30. Densities and Excess Volumes of the 1,3-Dimethylimidazolium Methylsulfate + Methanol System at Temperatures from (313.15 to 333.15) K and Pressures from (0.1 to 25) MPa
31. Excess molar volumes of N,N-dimethylformamide+2-pentanone+alkan-1-ols mixed solvent systems at 303.15K
32. Vapor−Liquid Equilibrium and Density of the Binary System 1-Phenylethylamine + Toluene
33. Prediction of Thermodynamic Properties of the Systems Formed by n-Alkanes, Aliphatic Monoethers, and 1-Chloroalkanes, Using a Cell−Hole Group Contribution Model
34. Vapor−Liquid Equilibria in Ethanol + (Butyl Methyl Ether or Dipropyl Ether) Systems at 308.15, 323.15, and 338.15 K
35. Thermodynamic properties of n-alcohol–n-alkane mixtures. A comparative study of some group contribution theories
36. Thermodynamics of alkanol–alkane systems. New modifications of the ERAS model
37. Excess heat capacities of alkan-1-ol–n-alkane systems at low alcohol concentrations. Description in terms of association
38. Determination of association constants for alcohols based on ethers as homomorphs
39. Thermodynamics of systems formed by any number of associating components
40. Solubility and vapour pressures in saturated solutions of high-molecular-weight hydrocarbons
41. A new method to determine association constants for alcohols from the properties of pure compounds
42. Correlations for the solubility of normal alkanoic acids ando-toluic acid in binary solvent mixtures
43. Solubility correlation of monocarboxylic acids in one-component solvents
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