Effect of attrition on particle size distribution and SO2 capture in fluidized bed combustion under high CO2 partial pressure conditions

Chemical Engineering Science

Volumn 65, Issue 1, 2010, Pages 550-555

  Saastamoinen, J J ^a   Shimizu, T ^b   Tourunen, A ^a  

^a VTT TECHNICAL RESEARCH CENTRE OF FINLAND   (Finland)

^b NIIGATA UNIVERSITY   (Japan)

Author keywords

Attrition; Fluidized beds; Particle; Population balance; Reaction engineering; SO2 capture

Indexed keywords

ATTRITION RATE; BED MATERIALS; BENCH-SCALE FLUIDIZED BED; DIFFUSION RESISTANCE; DIFFUSIVITIES; ELECTRIC ENERGIES; LIMESTONE PARTICLES; OXYGEN-ENRICHED; OXYGEN-ENRICHED COMBUSTION; PARTICLE; PARTICLE POPULATION; POPULATION BALANCE MODELS; PRODUCT LAYER; REACTION ENGINEERING; REACTION TIME; SHRINKING CORE MODEL; SULPHUR CAPTURE;

CARBON DIOXIDE; CARBON DIOXIDE PROCESS; DIFFUSION; FLUID DYNAMICS; FLUIDIZATION; FLUIDIZED BEDS; GAS EMISSIONS; GLOBAL WARMING; GREENHOUSE GASES; LEAKAGE (FLUID); LIMESTONE; OXYGEN; PARTICLE SIZE; PARTICLE SIZE ANALYSIS; REACTION RATES; SIZE DISTRIBUTION; SMOKE; SULFUR;

FLUIDIZED BED COMBUSTION;

EID: 71849118560     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2009.06.023     Document Type: Article

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