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Thiophene hydrogenolysis for the evaluation of hydrodesulfurization catalysts

Journal Article · · Ind. Eng. Chem. Process Des. Dev.; (United States)
DOI:https://doi.org/10.1021/i260067a016· OSTI ID:5318129

Thiophene hydrogenolysis at 400/sup 0/C and 1 atm in a vapor-phase, pulsed microcatalytic reactor was used to compare the hydrodesulfurization, olefin hydrogenation, and olefin isomerization functions of a commercial cobalt-molybdenum-alumina hydrodesulfurization catalyst, Harshaw 0402T, and two laboratory catalysts prepared by double impregnation of small- and large-pored aluminas. The small-pored catalyst had the highest hydrodesulfurization and olefin hydrogenation activity; the commercial catalyst was intermediate; the large-pored, the lowest. Sintering at 800/sup 0/ or 925/sup 0/C decreased catalyst activity. Catalyst presulfiding increased total thiophene conversion but decreased olefin hydrogenation. At 400/sup 0/C, the conversion over a 28-35 mesh commercial catalyst was 47%, but over a 10-80 mesh catalyst it was 55%. This particle size effect has possible implications for the use of cobalt-molybdenum-alumina catalysts in the hydrodesulfurization of coal or coal-derived liquids; substantially lower effectiveness factors may be expected in hydrotreating heavy liquids.

Research Organization:
State Univ., Buffalo, NY
OSTI ID:
5318129
Journal Information:
Ind. Eng. Chem. Process Des. Dev.; (United States), Journal Name: Ind. Eng. Chem. Process Des. Dev.; (United States) Vol. 17:3; ISSN IEPDA
Country of Publication:
United States
Language:
English