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Selectivity of coal minerals as catalysts in coal liquefaction and hydrodesulfurization

Conference · · Prepr. Pap. - Am. Chem. Soc., Div. Fuel Chem.; (United States)
OSTI ID:6140238
In the hydroliquefaction of a high-volatile Kentucky bituminous coal at 410/sup 0/C and 2000 psi hydrogen in light recycle oil, yields of oil, asphaltenes, preasphaltenes, and pyridine-insolubles were 32.6, 38.4, 16.6, and 12.5% with no catalyst; 57.4, 37.8, 4.8, and 0% with cobalt-molybdenum on alumina; 41.4, 38.5, 19.3, and 0.9% with metallic iron; and 33.0, 45.2, 12.8, and 9.1% with a solvent-refined coal (SRC) residue. Hydrogen consumption was greatly increased by coal ash and SRC residue though not as much as by the cobalt-molybdenum catalyst; iron had little effect on hydrogen consumption. For hydrodesulfurization, iron was about as effective as cobalt-molybdenum but was less selective for sulfur removal from the asphaltenes; coal ash and SRC residue were totally ineffective due to hydrogen sulfide poisoning. The effect of catalysis by SRC residue on the solvent refining process, particularly excess hydrogen consumption due to gas formation, is discussed. 15 references, tables.
Research Organization:
Auburn Univ., AL
OSTI ID:
6140238
Conference Information:
Journal Name: Prepr. Pap. - Am. Chem. Soc., Div. Fuel Chem.; (United States) Journal Volume: 22:6
Country of Publication:
United States
Language:
English