Effect of perforated ratios of distributor on the fluidization characteristics in a gas-solid fluidized bed

Industrial and Engineering Chemistry Research

Volumn 48, Issue 1, 2009, Pages 517-527

  Dong, Shuqin ^a   Cao, Changqing ^a   Si, Chongdian ^a   Guo, Qingjie ^a  

^a QINGDAO UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

[No Author keywords available]

Indexed keywords

AIR; COMPUTATIONAL FLUID DYNAMICS; CRACKING (CHEMICAL); DROPS; FLUID DYNAMICS; FLUIDIZATION; FLUIDIZED BEDS; GASES; PRESSURE DROP; VELOCITY;

BUBBLE SIZES; COMPUTATIONAL FLUID DYNAMICS CODES; CONCENTRATION PROFILES; EXPERIMENT VALUES; EXPERIMENTAL DATUM; FLUIDIZATION CHARACTERISTICS; GAS-PHASE; GAS-SOLID FLUIDIZED BEDS; NUMERICAL SIMULATIONS; PARTICLE CONCENTRATION DISTRIBUTIONS; PRESSURE-DRIVEN; ROOT MEAN SQUARES; SOLID HOLDUPS; SOLID PARTICLES; SOLID-PHASE; SUPERFICIAL GAS VELOCITIES;

FLUID CATALYTIC CRACKING;

EID: 61649108162     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie801073r     Document Type: Article

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