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Catalyst deactivation due to pore-plugging by reaction products. [In hydrotreating of residuum oils]

Conference · · Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States)
OSTI ID:7269901
In trickle-bed hydrodesulfurization the gas and liquid phases pass concurrent downflow over a fixed bed of catalyst. The hydrotreating of residuum oils at elevated temperatures and pressures in this way has revealed the presence of (undesirable) demetallation reactions taking place in parallel with the desired desulfurization reactions. Organometallic constituents of the oil, primarily vanadium, nickel and iron, react out of the oil and combine with hydrogen sulfide to produce solid deposits of metal sulfides. The deposition of the reaction products occur both inter- and intra-particle. The intra-particle deposits decrease the effective diffusivity of the catalyst causing deactivation by a pore-plugging mechanism. A simple model is proposed to take into consideration catalyst deactivation in residuum hydrotreating by metal sulfides build-up within the pores of the catalyst. The effect of the metal sulfides are considered the dominant feature of the deactivation process based on recent evidence from the literature. The demetallation rates used in the model are typical of current commercial practice. Predictions for catalyst life are compared with commercial data.
Research Organization:
Technical Univ. of Denmark, Bygning
OSTI ID:
7269901
Conference Information:
Journal Name: Am. Chem. Soc., Div. Fuel Chem., Prepr.; (United States) Journal Volume: 17:2
Country of Publication:
United States
Language:
English