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U.S. Department of Energy
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Kinetics and mechanism of catalytic hydroprocessing of components of coal-derived liquids. Fourth quarterly report, February 15, 1980-May 15, 1980

Technical Report ·
OSTI ID:5099670
An asphaltene-containing SRC-II coal liquid derived from Powhatan No. 5 mine coal and produced in the Ft. Lewis demonstration plant has been selected for study of catalytic hydroprocessing reactions. Analytical separation by liquid chromatography has been carried out to produce nine distinct fractions from 1 kg of coal liquid. These have been further separated into compound classes and characterized in detail by elemental analysis, mass spectrometry, NMR, and infrared spectroscopy. Compounds typical of each fraction (except asphaltenes) have been designated. Hydroprocessing of polynuclear aromatic hydrocarbons under industrially relevant conditions has shown that these are much more reactive than benzene. The reaction networks involve reversible hydrogenation and isomerization, and significant concentrations of hydroaromatic (hydrogen-donor) species are attainable under practical conditions. Hydroprocessing of solutions containing the following combinations of compounds has also been studied: quinoline/indole, quinoline/indole/dibenzothiophene, and quinoline/indole/naphthalene. Scanning electron microscopy combined with catalytic activity measurements was used to characterize deactivated and regenerated Ni-Mo-Al/sub 2/O/sub 3/ catalysts. EDAX results determined chemical composition of the catalyst and the deposited mineral crust. The results indicate that regeneration of the catalysts can recover much of the activity lost as a result of coke formation.
Research Organization:
Delaware Univ., Newark (USA). Dept. of Chemical Engineering; Gulf Research and Development Co., Pittsburgh, PA (USA)
DOE Contract Number:
AC22-79ET14880
OSTI ID:
5099670
Report Number(s):
DOE/ET/14880-04; ON: DE82019759
Country of Publication:
United States
Language:
English