Estudo de propriedades físicas de solventes eutécticos de origem natural

No contexto da utilização de solventes alternativos mais sustentáveis e eficientes, capazes de substituir solventes orgânicos convencionais que apresentam várias desvan-tagens tais como toxicidade, inflamabilidade, volatilidade, etc., foram propostos na lite-ratura várias alternativas entre as quais os solventes eutécticos de origem natural. Para potenciar a sua aplicação em diversas áreas, incluindo a tecnologia biomédica, é necessário estudar as suas propriedades físicas dada a ainda insuficiente base de dados disponível. Assim, o principal objetivo deste trabalho é efetuar a medição da massa vo-lúmica, da viscosidade e do índice de refração de solventes eutécticos de origem natural, formados por cloreto de colina e açúcares, ácidos orgânicos ou álcoois. Para isso, foram escolhidos quatro sistemas modelo, já propostos na literatura: glicerol + cloreto de coli-na + água (proporção molar 2:1:1); glucose + cloreto de colina + água (2:5:5); sacarose + cloreto de colina + água (1:4:4); ácido málico + cloreto de colina + água (1:1:2). Fo-ram ainda avaliados os efeitos da adição de água e/ou da temperatura nas diferentes propriedades físicas. A viscosidade dos solventes eutécticos foi medida entre 293,15 K e 323,15 K, para valores de fração mássica de água entre 5% e 30%. Nesta gama de temperatura, os da-dos experimentais foram modelizados de forma satisfatória por uma equação do tipo Arrhenius. Como esperado, a viscosidade diminuiu com o aumento da temperatura e com o aumento de conteúdo em água. De facto, um aumento da temperatura de 20 °C para 50 °C traduz-se numa diminuição muito significativa da viscosidade dos solventes estudados. O índice de refração foi medido à temperatura de 298,15 K, obtendo-se valores na gama 1,41-1,50. Finalmente, a massa volúmica foi medida entre 298,15 K e 333,15 K. Verifica-se que, nas condições estudadas, a massa volúmica diminui linearmente com a temperatura e com o aumento da fração mássica de água, sendo muito menos sensível ao conteúdo em água ou à temperatura do que a viscosidade.

Vapor–liquid equilibrium of binary mixtures containing isopropyl acetate and alkanols at 101.32 kPa

Isobaric vapor-liquid equilibria of binary mixtures of isopropyl acetate plus an alkanol (1-propanol, 2-propanol, 1-butanol, or 2-butanol) were measured at 101.32 kPa, using a dynamic recirculating still. An azeotropic behavior was observed only in the mixtures of isopropyl acetate + 2-propanol and isopropyl acetate + 1-propanol. The application of four thermodynamic consistency tests (the Herington test, the Van Ness test, the infinite dilution test, and the pure component test) showed the high quality of the experimental data. Finally, both NRTL and UNIQUAC activity coefficient models were successfully applied in the correlation of the measured data, with the average absolute deviations in vapor phase composition and temperature of 0.01 and 0.16 K, respectively.

Measurements of activity coefficients at infinite dilution of organic solutes and water on polar imidazolium-based ionic liquids

The activity coefficients at infinite dilution, gamma(infinity)(13), of 55 organic solutes and water in three ionic liquids with the common cation 1-butyl-3-methylimidazolium and the polar anions Cl--,Cl- [CH3SO3](-) and [(CH3)(2)PO4](-), were determined by (gas + liquid) chromatography at four temperatures in the range (358.15 to 388.15) K for alcohols and water, and T = (398.15 to 428.15) K for the other organic solutes including alkanes, cycloalkanes, alkenes, cycloalkenes, alkynes, ketones, ethers, cyclic ethers, aromatic hydrocarbons, esters, butyraldehyde, acetonitrile, pyridine, 1-nitropropane and thiophene. From the experimental gamma(infinity)(13) values, the partial molar excess Gibbs free energy, (G) over bar (E infinity)(m), enthalpy (H) over bar (E infinity)(m), and entropy (S) over bar (E infinity)(m), at infinite dilution, were estimated in order to provide more information about the interactions between the solutes and the ILs. Moreover, densities were measured and (gas + liquid) partition coefficients (KL) calculated. Selectivities at infinite dilution for some separation problems such as octane/benzene, cyclohexane/benzene and cyclohexane/thiophene were calculated using the measured gamma(infinity)(13), and compared with literature values for N-methyl-2-pyrrolidinone (NMP), sulfolane, and other ionic liquids with a common cation or anion of the ILs here studied. From the obtained infinite dilution selectivities and capacities, it can be concluded that the ILs studied may replace conventional entrainers applied for the separation processes of aliphatic/aromatic hydrocarbons.

Solubility and solvation of monosaccharides in ionic liquids

Herein, solubility experimental data for six monosaccharides, viz. D-(+)-glucose, D-(+)-mannose, D-(-)-fructose, D-(+)-galactose, D-(+)-xylose and L-(+)-arabinose, in four ionic liquids (ILs), at temperatures ranging from 288.2 to 348.2 K, were obtained aimed at gathering a better understanding of their solvation ability and molecular-level mechanisms which rule the dissolution process. To ascertain the chemical features that enhance the solubility of monosaccharides, ILs composed of dialkylimidazolium or tetra-alkylphosphonium cations combined with the dicyanamide, dimethylphosphate or chloride anions were investigated. It was found that the ranking of the solubility of monosaccharides depends on the IL; yet, D-(+)-xylose is always the most soluble while D-(-)-fructose is the least soluble monosaccharide. The results obtained show that both the IL cation and the anion play a major role in the solubility of monosaccharides. Finally, from the determination of the respective thermodynamic properties of solution, it was found that enthalpic contributions are dominant in the solubilization process. However, the observed differences in the solubilities of monosaccharides in 1-butyl-3-methylimidazolium dicyanamide are ruled by a change in the entropy of solution.