Centrifugal fluidized combustion of coal. Quarterly report, January--March 1977. [2 refs]
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
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Related Subjects
01 COAL, LIGNITE, AND PEAT
014000* -- Coal
Lignite
& Peat-- Combustion
42 ENGINEERING
421000 -- Engineering-- Combustion Systems
BURNERS
CARBONACEOUS MATERIALS
CENTRIFUGATION
CHEMICAL REACTIONS
COAL
COMBUSTION
COMBUSTORS
DESIGN
ENERGY SOURCES
FLOW RATE
FLUID FLOW
FLUIDIZED-BED COMBUSTION
FLUIDIZED-BED COMBUSTORS
FORECASTING
FOSSIL FUELS
FUELS
GAS FLOW
OXIDATION
PRESSURE DROP
SEPARATION PROCESSES
TESTING
THERMOCHEMICAL PROCESSES
014000* -- Coal
Lignite
& Peat-- Combustion
42 ENGINEERING
421000 -- Engineering-- Combustion Systems
BURNERS
CARBONACEOUS MATERIALS
CENTRIFUGATION
CHEMICAL REACTIONS
COAL
COMBUSTION
COMBUSTORS
DESIGN
ENERGY SOURCES
FLOW RATE
FLUID FLOW
FLUIDIZED-BED COMBUSTION
FLUIDIZED-BED COMBUSTORS
FORECASTING
FOSSIL FUELS
FUELS
GAS FLOW
OXIDATION
PRESSURE DROP
SEPARATION PROCESSES
TESTING
THERMOCHEMICAL PROCESSES