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Kinetics and mechanism of desulfurization and denitrogenation of coal-derived liquids. Seventh quarterly report, December 21, 1976--March 20, 1977. [CoO--MoO3 and NiO--MoO3]

Technical Report ·
DOI:https://doi.org/10.2172/5295310· OSTI ID:5295310
Three high-pressure flow microreactors and two batch autoclave reactors have been used to study the reaction networks and kinetics of (1) catalytic hydrodesulfurization of dibenzothiophene and methyl-substituted dibenzothiophenes and (2) catalytic hydrodenitrogenation of acridine. The catalysts were commercial, sulfided CoO-MoO/sub 3//..gamma..-Al/sub 2/O/sub 3/ and commercial, sulfided NiO-MoO/sub 3//..gamma..-Al/sub 2/O/sub 3/. At 300/sup 0/C and 104 atm, dibenzothiophene reacts to give H/sub 2/S and biphenyl in high yield. Methyl-substituted dibenzothiophenes react similarly, and each reaction is first-order in the sulfur-containing compound. Two methyl groups near the sulfur atom (in the 4 and 6 positions) reduce the reactivity tenfold, whereas methyl groups in positions further removed from the sulfur atom increase reactivity about twofold. These results are consistent with steric and inductive effects. In acridine conversion, a large amount of hydrogenation precedes nitrogen removal. Breaking of the carbon-nitrogen bond is evidently part of the slowest reaction in the network. The Ni-Mo catalyst is about twice as active as the Co-Mo catalyst for ring hydrogenation, and the two catalysts are about equally active for breaking the carbon-nitrogen bond. Aged catalysts taken from the H-Coal process had greatly reduced activity.
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:
5295310
Report Number(s):
FE-2028-8
Country of Publication:
United States
Language:
English