Abstract
Small pore zeolites have shown great potential in a number of catalytic reactions. While Mo-containing medium pore zeolites have been widely studied for methane dehydroaromatisation (MDA), the use of small pore supports has drawn limited attention due to the fast deactivation of the catalyst. This work investigates the structure of the small pore Mo/H-SSZ-13 during catalyst preparation and reaction by operando X-ray absorption spectroscopy (XAS), in situ synchrotron powder diffraction (SPD), and electron microscopy; then, the results are compared with the medium pore Mo/H-ZSM-5. While SPD suggests that during catalyst preparation, part of the MoOx anchors inside the pores, Mo dispersion and subsequent ion exchange was less effective in the small pore catalyst, resulting in the formation of mesopores and Al2(MOO4)3 particles. Unlike Mo/H-ZSM-5, part of the Mo species in Mo/H-SSZ-13 undergoes full reduction to Mo0 during MDA, whereas characterisation of the spent catalyst indicates that differences also exist in the nature of the formed carbon deposits. Hence, the different Mo speciation and the low performance on small pore zeolites can be attributed to mesopores formation during calcination and the ineffective ion exchange into well dispersed Mo-oxo sites. The results open the scope for the optimisation of synthetic routes to explore the potential of small pore topologies.
Highlights
Methane dehydroaromatisation (MDA) reaction converts methane directly into aromatics and light hydrocarbons, giving H2 as a co-product
Mass spectrometry results revealed a decreased benzene formation on small pore Mo/H-SSZ-13 catalyst; besides, higher carbon deposit content was detected for the 90 min spent Mo/H-SSZ-13 (6.2 wt %) catalyst as compared with the widely investigated Mo/H-ZSM-5 (3.0 wt %)
To gain insight into such a fast deactivation process, structural differences in both catalysts were evaluated by operando X-ray absorption spectroscopy (XAS) experiments
Summary
Methane dehydroaromatisation (MDA) reaction converts methane directly into aromatics and light hydrocarbons, giving H2 as a co-product. Since the first report on MDA by Wang et al [1], most of the catalysts studied for this reaction comprise Mo supported in medium pore H-ZSM-5 zeolite with. The extensive work performed in Mo/H-ZSM-5 include the optimisation of synthetic procedures [3,4,5,6], modelling studies [7,8,9,10], the development of engineering solutions [11,12,13], and structural investigations to study the active role of Mo, zeolite, or carbon deposits [14,15,16,17,18,19,20,21,22,23,24,25,26,27]. Good catalytic performance and significant yield to aromatics have been reported for non-microporous supports [30]
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