Modeling of NO removal over CuO/γ-Al2O3 catalyst in a bubbling fluidized bed reactor

Industrial and Engineering Chemistry Research

Volumn 48, Issue 17, 2009, Pages 7959-7964

  Irfan, Muhammad F ^b   Kim, Sang Done ^b   Usman, Muhammad R ^a  

^a Korea Advanced Institute of Science and Technology (KAIST)   (South Korea)

^b UNIVERSITY OF THE PUNJAB   (Pakistan)

Author keywords

[No Author keywords available]

Indexed keywords

ADSORPTION/DESORPTION; BED MATERIALS; BUBBLING FLUIDIZED BED; BUBBLING FLUIDIZED BED REACTOR; FLUIDIZED BED REACTORS; MATLAB SIMULATIONS; MOLAR RATIO; NO REDUCTION; NO REMOVAL; PHASE THEORY; REACTION TEMPERATURE; REDUCTION EFFICIENCY; SIMULATION RESULT; STATIC BED HEIGHT; SUPERFICIAL GAS VELOCITIES; TWO-PHASE MODEL;

ALUMINUM; BUBBLE FORMATION; CATALYSIS; CATALYSTS; CHEMICAL REACTORS; FLUID CATALYTIC CRACKING; FLUID DYNAMICS; FLUIDIZATION; FLUIDIZED BED FURNACES; FLUIDIZED BEDS; MATLAB; RATE CONSTANTS; REDUCTION; SIMULATORS;

FLUIDIZED BED PROCESS;

EID: 69949126513     PISSN: 08885885     EISSN: None     Source Type: Journal    
DOI: 10.1021/ie8018214     Document Type: Article

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