Microwave-assisted partial hydrogenation of citral by using ionic liquid-coated porous glass catalysts.

The microwave-assisted hydrogenation of citral (3,7-dimethylocta-2,6-dienal) to citronellal with molecular hydrogen as the reducing agent was investigated. Several polar and non-polar solvents were screened and imidazolium-based ionic liquids were applied as modifiers for the palladium-containing porous glass catalysts (Pd/TP). The best results were obtained with N-ethyl-N'-methylimidazolium dicyanamide, N-ethyl-N'-methylimidazolium acetate, or N-ethyl-N'-methylimidazolium trifluoroacetate, which were used to prepare supported catalysts with an ionic liquid layer (SCILL) on Pd/TP by wet-impregnation. The influence of pressure and temperature when using these ionic liquid-containing catalysts, as well as their long-term stabilities, were examined. Working with microwave-assisted heating, high yields of citronellal were achieved under mild conditions within short reaction times. Catalyst characterization was carried out by means of BET measurements, X-ray photoelectron spectroscopy (XPS) and thermo-gravimetric analyses. The influences of the ionic liquid layer were derived from experiments carried out before and after the reactions.

(2)H and (19)F solid-state NMR studies of the ionic liquid [C(2)Py][BTA]-d(10) confined in mesoporous silica materials.

Ionic liquids confined in porous materials are important solvents which allow a simple heterogenization of homogenous liquids. The perdeuterated ionic liquid N-ethylpyridinium-bis(trifluoromethanesulfonyl)amide ([C(2)Py][BTA]-d(10)) was prepared and its bulk phase behavior was studied by differential scanning calorimetry (DSC) and temperature-resolved (2)H and (19)F solid-state NMR spectroscopy. Its bulk properties were compared to [C(2)Py][BTA]-d(10) confined in a mesoporous silica support material as model material usable in SILP catalysts. The line shape analysis of the temperature-dependent NMR spectra of the bulk material reveals two phase transitions, one at 287-289 K (solid II/solid I) and one extending over a temperature range of 298-306 K (solid I/liquid). While the first phase transition is caused by the onset of an intramolecular rotation of the ethyl group of the cation, the second is due to the melting of the ionic liquid. In the bulk material, a hysteresis between the transition temperatures in heating and cooling scans occurs. In confinement, the dynamics of the ionic liquid changes considerably: no hysteresis is observed for [C(2)Py][BTA]-d(10) confined in the mesopores. Instead, only a broad transition from solid II to the liquid state, which spans the temperature range of 215-245 K, is observed. This transition is identified as the result of a broad distribution of molecular environments of the confined ionic liquid, which thus forms an amorphous phase inside the pores. Hence, the behavior of the ionic liquid in confinement is similar to the behavior of non-ionic guest molecules in the mesoporous silica. Finally, it was found that the anion and cation of the ionic liquid exhibit the same dynamic behavior in confinement.

Para-hydrogen induced polarization in homogeneous phase--an example of how ionic liquids affect homogenization and thus activation of catalysts.

Para-hydrogen induced polarization (PHIP) is observed in an organic solvent-free homogeneous catalyst/substrate system using ionic liquids. The hydrogenation reactions are performed employing a Rh-catalyst/ionic liquid system without further organic solvents. The PHIP phenomenon is demonstrated for the ethyl acrylate system. Small amounts of ionic liquids (ILs) containing weakly coordinating anions such as [Tf2N]- act as homogenizing cosolvents for the catalyst in ethyl acrylate, leading to a dramatic activation of the catalytic process and a high PHIP signal enhancement. The achieved enhancement depends strongly on the viscosity of the ethyl acrylate/IL mixture. Furthermore, by deliberate choice of the IL constituents it was possible to design a model system exhibiting both sufficient catalyst solubility and biphasic liquid-liquid behavior. This shows that in ionic liquids PHIP enhancements followed by a fast quantitative removal of the para-hydrogenated product from the catalyst phase is in principle possible. The possible PHIP enhancement factors will depend strongly on the design of a suitable hydrogenation reactor.