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U.S. Department of Energy
Office of Scientific and Technical Information

Kinetics and mechanism of desulfurization and denitrogenation of coal-derived liquids. Quarterly report, June 20, 1976--September 19, 1976

Technical Report ·
DOI:https://doi.org/10.2172/7214620· OSTI ID:7214620

Two high-pressure flow microreactors are functioning efficiently in studies of dibenzothiophene hydrodesulfurization and quinoline hydrodenitrogenation. Assembly of a third microreactor is scheduled for completion in about three months. Dibenzothiophene hydrodesulfurization at conditions such as 1,000 psig and 300-350/sup 0/C takes place in the absence of mass transfer influence. The rate is surprisingly high, requiring temperatures of 300/sup 0/C or less for determination of differential conversions with the existing apparatus. Batch reaction studies have shown that nitrogen removal from quinoline is characterized by an apparent activation energy of about 20 kcal/mole, whereas the rates of accompanying hydrogenation reactions are almost independent of temperature. Nitrogen removal from acridine and from carbazole is much slower than nitrogen removal from quinoline; the outer rings of the three ring compounds (acridine and carbazole) are hydrogenated relatively rapidly.

Research Organization:
Delaware Univ., Newark (USA)
Sponsoring Organization:
US Energy Research and Development Administration (ERDA)
DOE Contract Number:
EX-76-C-01-2028
OSTI ID:
7214620
Report Number(s):
FE-2028-6
Country of Publication:
United States
Language:
English