Investigation into a gas-solid-solid three-phase fluidized-bed carbonator to capture CO2 from combustion flue gas

Chemical Engineering Science

Volumn 66, Issue 3, 2011, Pages 375-383

  Cao, Changqing ^a   Zhang, Kai ^a   He, Chenchen ^a   Zhao, Yanan ^a   Guo, Qingjie ^a  

^a QINGDAO UNIVERSITY OF SCIENCE AND TECHNOLOGY   (China)

Author keywords

Chemical reactors; CO2 capture; Combustion flue gas; Conversion; Dynamic simulation; Fluidization

Indexed keywords

CAPTURE EFFICIENCY; CFD SOFTWARES; CO2 CAPTURE; COMBUSTION FLUE GAS; CONVERSION; CYCLE NUMBER; DYNAMIC BEHAVIORS; DYNAMIC SIMULATION; EXPERIMENTAL MEASUREMENTS; GAS-SOLID; HYDRODYNAMIC CHARACTERISTICS; LOCAL HYDRODYNAMICS; LOCAL TIME; MODEL SIMULATION; MOLAR FRACTIONS; OPERATING CONDITION; OPERATION CONDITIONS; REACTION TEMPERATURE; THREE PHASE FLUIDIZED BED; TRANSIENT MODEL;

CHEMICAL REACTIONS; CHEMICAL REACTORS; CHEMICALS; COMPUTATIONAL FLUID DYNAMICS; COMPUTER SIMULATION; FLUE GASES; FLUES; FLUID DYNAMICS; FLUIDIZED BED COMBUSTION; FLUIDIZED BEDS; GASES; HYDRODYNAMICS; REACTION RATES;

FLUIDIZATION;

EID: 78650703843     PISSN: 00092509     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ces.2010.10.028     Document Type: Article

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