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U.S. Department of Energy
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Rate enhancement for catalytic upgrading coal naphthas. Quarterly progress report for period ending, September 1993

Technical Report ·
DOI:https://doi.org/10.2172/10141086· OSTI ID:10141086
The hydrotreatment of naphtha derived from Illinois {number_sign}6 coal has been carried out over unsupported transition metal sulfide catalysts of the second row of the Periodic Table. The catalysts prepared are similar to the catalysts prepared by Pecoraro and Chianelli (1981). The catalysts exhibit a volcano curve for the HDS of dibenzothiophene similar to that observed by Pecoraro and Chianelli (1981). The catalysts also exhibit similar volcano curves for the HDS, HDN and HDO of the total sulfur, nitrogen and oxygen heteroatoms present in coal-derived naphtha. Ruthenium sulfide is the most active catalyst for all three of these processes. The order of reactivity for HDS, HDN and HDO is Ru > Rh > Mo > Pd > Zr > Nb. The kinetics of total sulfur and nitrogen removal from the coal-derived naphtha are quite complex. The conversion versus residence time data do not fit simple zero or first order kinetics. The individual sulfur compounds present in naphtha exhibit considerable interconversion indicating that C-C bond breaking and hydrogenation of aromatic rings are involved during HDS. The individual nitrogen compounds present in naphtha show that anilines are intermediates in the HDN of nitrogen compounds.
Research Organization:
Kentucky Univ., Lexington, KY (United States). Center for Applied Energy Research
Sponsoring Organization:
USDOE, Washington, DC (United States)
DOE Contract Number:
AC22-91PC91058
OSTI ID:
10141086
Report Number(s):
DOE/PC/91058--T8; ON: DE94009697; BR: AA2560000
Country of Publication:
United States
Language:
English