A systematic change of HZSM-5 (HZ5)
as a catalyst of the methanol
to aromatics (MTA) reaction was undertaken by employing a fixed-bed
tubular-type reactor under ambient pressure, applying a weight hourly
space velocity (WHSV) of 2 h–1 at 375 °C, as
the first report on the application of low-Si/Al-ratio alkaline-[Mo,Na]-HZSM-5
in the MTA process. To characterize the surface and textural properties
of the catalysts, powder X-ray diffraction (PXRD), nitrogen adsorption/desorption,
temperature-programmed desorption of ammonia (NH3-TPD),
pyridine-infrared spectroscopy (Py-IR), thermogravimetric analysis
(TGA), and energy-dispersive X-ray (EDX) methods were employed. Gas
chromatography (GC) and gas chromatography-mass spectrometry (GC-MS)
measurements demonstrated a selectivity of up to 86 wt % (65.7 wt
% for benzene, toluene, and xylene (BTX)) over 2[Mo]HZ5.
NH3-TPD and Py-IR results indicated a sensible decrease
of strong acid sites on the impregnated samples, while the surface
analyses revealed the highest Lewis acid sites (LAS) together with
the largest mesopore surface area for 2[Mo]alk-HZ5, supporting
the migration of Mo species to the bulk of the catalysts. Mo impregnation
had a minor effect on the observed coke formation in the promoted
catalyst.