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Zeolite catalysts for hdyrocracking polynuclear aromatics - phenanthrene kinetics

Thesis/Dissertation ·
OSTI ID:6346408
Three zeolite-based catalysts were tested for the hydrocracking reaction of polynuclear aromatics (phenanthrene) by using the gradientless Berty-type reactor at three different temperatures (258/sup 0/C, 281/sup 0/C, and 298/sup 0/C) and 95 atm. operating pressure. Three commercially used silica-alumina-based catalysts were also tested at the same operating conditions for the purpose of comparison. The experimental studies were made to determine the catalytic activity of three zeolite-based catalysts, the kinetic scheme of hydrocracking reaction of phenanthrene, to compare the activity of the amphorous silica-alumina catalyst and zeolite-based catalyst in the hydrocracking reaction of polynuclear aromatic compounds, and to evaluate the activity of the zeolite-based catalyst for upgrading coal-derived liquids and shale-oil derived liquids. The hydrocracking phenanthrene activity of zeolite-based catalyst is greater than that of silica-alumina-based catalysts. The hydrocracking phenanthrene activity increases with the order CoMo sulfides < Ni-Mo sulfides < Ni-W sulfides of bimetallic combinations. Ni-W/USY is the most active catalyst in all six-tested catalysts. The deactivation rate of the catalyst is minimal for the zeolite-based catalysts. On the other hand, the deactivation rate is high in the silica-alumina-based catalysts under similar operating conditions as zeolite-based catalysts. A Langmuir-Hinshelwood dual-site mechanisms is the best model to describe the hydrocracking reaction of polynuclear aromatics over zeolite-based catalysts.
OSTI ID:
6346408
Country of Publication:
United States
Language:
English