Comparison on process efficiency for CLC of syngas operated in packed bed and fluidized bed reactors

International Journal of Greenhouse Gas Control

Volumn 28, Issue , 2014, Pages 65-78

  Hamers, H P ^a   Romano, M C ^b   Spallina, V ^a   Chiesa, P ^b   Gallucci, F ^a   Annaland, M Van Sint ^a  

^a EINDHOVEN UNIVERSITY OF TECHNOLOGY   (Netherlands)

^b POLITECNICO DI MILANO   (Italy)

Author keywords

Chemical looping combustion; Fluidized beds; Integrated Gasification Combined Cycles (IGCC); Packed beds; Process efficiency

Indexed keywords

CHEMICAL REACTORS; COAL COMBUSTION; COST ESTIMATING; EFFICIENCY; FLUIDIZATION; FLUIDIZED BED FURNACES; FLUIDIZED BED PROCESS; FLUIDIZED BEDS; FUELS; NICKEL OXIDE; OXYGEN; PACKED BEDS; SUPERSATURATION; SYNTHESIS GAS; CARBON DIOXIDE;

CHEMICAL LOOPING COMBUSTION; CIRCULATING FLUIDIZED BED; CIRCULATING FLUIDIZED BED REACTOR; HIGH TEMPERATURE AND HIGH PRESSURE; INTEGRATED GASIFICATION COMBINED CYCLE; OVERALL PROCESS EFFICIENCIES; PROCESS EFFICIENCY; TEMPERATURE DIFFERENCES; CO2 CAPTURE;

FLUIDIZED BED COMBUSTION;

BIOREACTOR; CARBON MONOXIDE; CARBON SEQUESTRATION; COMBUSTION; ENTHALPY; HYDROGEN; OXIDATION; OXYGEN; TEMPERATURE GRADIENT; CARBON DIOXIDE; CHEMICAL PROCESS; COMPARATIVE STUDY;

EID: 84903694667     PISSN: 17505836     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.ijggc.2014.06.007     Document Type: Article

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