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The characterization of acid sites on solid catalysts is a key to understanding reaction mechanisms at the molecular level. This is generally done indirectly using a model probe molecule able to coordinate or be protonated on surface acid sites. For instance, Temperature Programmed Desorption (TPD) of the pyridine probe molecule followed by IR spectroscopy has become a standard method for the quantification and identification of Brønsted and Lewis acid sites found in zeolites. On the other hand, there is a lack of molecules able to be protonated on very weak Brønsted acid sites. In this work 2,6-ditert- butylpyridine is shown to be a suitable probe for characterizing weak Brønsted acidity. The proof of concept is performed on a series of Pt catalysts supported on a chlorinated alumina support (Pt--γ-Al2O3--Cl) generally used in the reforming process. In particular, we show that the area of the 1617 cm-1 vibration band is correlated to the concentration of Cl introduced into the catalyst. We also underline the relative insensitivity of pyridine as an IR probe molecule and the inadequacy of NH3 TPD for the characterization of acid sites of reforming catalysts, making 2,6-di-tert-butylpyridine a particularly important and specific probe molecule. [ABSTRACT FROM AUTHOR]

A simple kinetic model based on the zeolite acid strength, the number of Brønsted acid sites, and the catalyst efficiency was developed for the cracking of n-hexane. A series of HY zeolites with a mesopore volume from 0.04 to 0.32 cm3/g was synthesized and characterized by various physical-chemical methods and tested for n-hexane cracking. The generation of mesoporosity influenced several other important parameters, such as acidity and extra-framework aluminum. Zero-length column diffusion measurements for mesitylene showed a large decrease in the characteristic diffusion time upon the introduction of mesoporosity, which changed only slightly with a further increase in mesoporosity. Similar n-hexane physisorption enthalpies were measured for all samples. The highest initial activity for n-hexane cracking per catalyst volume was observed for the sample with an intermediate mesopore volume of 0.15 cm3/g. The three mesoporous H-USY zeolites showed the same value of the intrinsic rate constant and the same activation energy. The difference in initial activity of the mesoporous zeolites was caused by the difference in the number of Brønsted acid sites. The increase in initial activity for the mesoporous zeolites compared to a microporous zeolite was caused by an increase in the acid strength. [ABSTRACT FROM AUTHOR]