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U.S. Department of Energy
Office of Scientific and Technical Information

Research and development of rapid hydrogenation for coal conversion to synthetic motor fuels (riser cracking of coal). Project 61001 annual report, April 1, 1978-March 31, 1979

Technical Report ·
OSTI ID:5699630
The effects of operating pressure and heating rate on reactor performance were studied. In addition, several techniques for processing caking coals were explored, and trials of bentonite clay and iron oxide as catalysts were made. In the bench-scale unit program, the main findings can be summarized as follows: At low operating pressure, carbon conversion is low, and increases as operating pressure increases; at high heating rates with negligible residence time at maximum temperature, carbon conversions are reduced, and phenols and cresols form a substantial fraction of the hydrocarbon liquid products; over the range of heating rates studied thus far, liquid yields are better at lower heating rates; in a cocurrent heating mode, the distribution of carbon among products was found to correlate with severity function; unpretreated caking coals can be processed using silica sand or char as inert diluents; caking coal can be pretreated with lime under mild conditions and successfully processed in the bench-scale unit; both bentonite clay and iron oxide have potential catalytic effects, allowing good carbon conversions at low hydrogen to-coal weight ratios. Some support studies were made using the bench-scale unit and other equipment to clarify certain aspects of the PDU in the operation of the preheater and in the operation of the combustor sections. The main findings from these studies are summarized.
Research Organization:
Institute of Gas Technology, Chicago, IL (USA)
OSTI ID:
5699630
Report Number(s):
FE-2307-50
Country of Publication:
United States
Language:
English