Skip to main content
U.S. Department of Energy
Office of Scientific and Technical Information

Centrifugal fluidized combustion of coal. Quarterly report, January--March 1977. [2 refs]

Technical Report ·
DOI:https://doi.org/10.2172/7219323· OSTI ID:7219323
Experiments with tapered distributors show strong effects of distributor angle, grid pressure drop, angular velocity, and bed mass on startup, minimum fluidization and bed pressure drop. Analyses were developed to predict the influence of these factors on system performance. Comparisons of preliminary theoretical results with available data are presented.
Research Organization:
Lehigh Univ., Bethlehem, PA (USA)
OSTI ID:
7219323
Report Number(s):
FE-2516-2
Country of Publication:
United States
Language:
English