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Flash pyrolysis of Chattanooga oil shale

Conference · · Proceeding, Eastern Oil Shale Symposium; (United States)
OSTI ID:6264418
Flash pyrolysis of Chattanooga oil shale was conducted in an entrained-solids reactor using N/sub 2/ as the entrainer at atmospheric pressure and temperatures from 485 to 685/sup 0/C. The residence time in the reactor was 8 sec. The particle sizes of the shale used were -40 +50 and -50 +70 mesh. The raw oil shale assayed 10.8 gal/ton and the maximum oil yield from the flash pyrolysis experiments was 70% of the modified Fischer assay yield at a temperature of 485/sup 0/C. The maximum oil yield was at the lowest temperature run, which gave a carbon conversion of 40%. At the optimum conditions, 14% of the carbon in the raw shale was converted to gaseous products, while at the highest temperatures 55% was converted to gas. Higher retorting temperatures favor gas production rather than oil production. Hydrogen constituted over 90 mole% of the gas produced (on a nitrogen-free basis) at the condition of maximum oil yield, while carbon oxides were less than 2%. The oil produced contained approximately 4% sulfur, which was less than 3% of the sulfur in the raw oil shale. Further processing of the shale is required to recover the energy contained in the carbon residue on the spent shale.
Research Organization:
Univ. of Alabama, University
OSTI ID:
6264418
Report Number(s):
CONF-8411130-
Conference Information:
Journal Name: Proceeding, Eastern Oil Shale Symposium; (United States) Journal Volume: IMMR84/124
Country of Publication:
United States
Language:
English