Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Commercial scale expanded bed hydroprocessing of Solvent Refined Coal (SRC) extract. October monthly technical progress report. [Ni/Mo, Co/Mo, Ni/W]

Technical Report ·
DOI:https://doi.org/10.2172/5294764· OSTI ID:5294764
Catalyst screening runs of two additional commercially available desulfurization/denitrogenation catalysts (Ni/Mo-B and Ni/Mo-C) have been completed. A total of three nickel-molybdenum, two cobalt-molybdenum, and one nickel-tungsten catalyst was included in the catalyst screening program. Within the constraints of the 10-day maximum run duration for individual catalyst screening runs, the nickel-molybdenum catalyst (Ni/Mo-A) was the best catalyst tested to date for desulfurization and denitrogenation (approximately 75 weight percent pseudo-conversion of 850/sup 0/F+ material at a denitrogenation activity of approximately 75 percent). After eight 24-hour periods of operation for Run LCF-33 (Ni/Mo-B), the average reactor temperatures were raised in two steps to 840/sup 0/F to 810 to 825, then 825 to 840/sup 0/F. The apparent effect of increased temperature was merely to arrest the loss of denitrogenation activity which was occurring during the first eight periods. However, when the data was normalized to 810/sup 0/F, it was noted that the catalyst still showed a loss in denitrogenation activity at constant temperature. The Ni/Mo-A catalyst was chosen as the candidate for the 30-day catalyst aging run. The aging run is currently under investigation and has progressed through period 5.
Research Organization:
Cities Service Oil Co., Tulsa, Okla. (USA)
OSTI ID:
5294764
Report Number(s):
FE-2038-18
Country of Publication:
United States
Language:
English