Deactivation by coke deposition on the HZSM-5 catalysts in the methanol-to-hydrocarbon conversion

HZSM-5 used to be the main catalyst component for the MTG process of Exxonmobil Co. Catalyst deactivation by coke in methanol-to-hydrocarbon (MTH) over HZSM-5 was studied in a fixed-bed reactor by observing the activity and selectivity with time-on-stream at 500 °C and WHSV=4.25 h−1. The HZSM-5 with SiO2/Al2O3 ratios of 40 and 280 were synthesized and characterized with XRD, N2 adsorption/desorption and NH3-TPD. The used catalysts were investigated by N2 adsorption/desorption, XRD, elemental analysis (EA) and UV–vis spectroscopy to identify the nature of coke. If the acidity of HZSM-5 is low (SiO2/Al2O3=280), the coke deposited is mainly mono- or bi-aromatic which did not affect the catalyst activity significantly. On the other hand when the acidity is high (SiO2/Al2O3=40), the coke deposited is polycyclic aromatics with 3 or 4 fused rings which leads to significant deactivation after 24 h. It is presumed that the coke on the HZSM-5 with low acidity must be located inside the pores and/or in the framework, since the coke particles without polycyclic aromatics should be small. The deactivation of HZSM-5 with high acidity is mainly caused by the bulky coke molecules, most probably inducing the topological blocking of the zeolite pores and channels.

► HZSM-5 with different acidities for methanol-to-hydrocarbon conversion.
► Hzsm-5 with high acidity showed catalytic deactivation by coke after 24 h.
► The coke deposited is polycyclic aromatic with 3 or 4 fused rings.
► Topological blocking of the pores and channels by the bulky coke molecules.