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Catalytic activity of coal minerals in coal liquefaction

Conference · · 84th AICHE Natl. Meet. Prepr.; (United States)
OSTI ID:6894072
Activity is studied in a tubing-bomb reactor with charges of 2.4 g coal and 4.8 g solvent and in an autoclave with charges of 40 g coal and 80 g solvent. Highly volatile bituminous coals (Kentucky No. 9/14 or Illinois No. 6) were hydrogenated with either tetralin or light recycle oil (LRO) from the Wilsonville SRC (Solvent Refined Coal) pilot plant. The major role of catalysts appears to be the replenishment of hydrogen donor species in the solvent, which is the over-all rate-limiting step in coal liquefaction. Addition or recycle of iron as SRC residue ash in the process stream may be advantageous, because it is an active catalyst in both hydrogenation and hydrodesulfurization and has an ability for H/sub 2/S removal by direct reaction. Adequate yield and desulfurization are attainable at lower temperature and perhaps lower pressure if mineral catalysis is used. Hydrogen consumption can also be significantly reduced when operating at lower temperature with a mineral catalyst.
Research Organization:
Auburn Univ.
OSTI ID:
6894072
Report Number(s):
CONF-780223-
Conference Information:
Journal Name: 84th AICHE Natl. Meet. Prepr.; (United States) Journal Volume: 51B
Country of Publication:
United States
Language:
English