Abstract
Carbon capture and storage is a concept to reduce greenhouse gas
emissions of energy production from fossil fuels. In oxy‐fuel
combustion, the fuel is burned in a mixture of oxygen and recycled flue
gas. This generates CO2‐rich flue gas from which the CO2
is easily separated and compressed. Foster Wheeler Power Group is
developing the existing design tools and process models of air‐fired
circulating fluidized bed boilers to implement specific features of
oxycombustion. The validation data is produced from bench‐scale and
pilot‐scale experiments at the VTT, Technical Research Centre of
Finland. A three‐dimensional circulating fluidized bed (CFB) furnace
model is developed and applied by Lappeenranta University of Technology
for predicting the effects of oxycombustion in full scale units. This
paper presents concept studies and initial 3D modeling results based on a
460 MWe supercritical CFB power plant at Lagisza, and
pilot‐scale studies with flue gas recirculation demonstrating real
oxygen combustion conditions.
Original language | English |
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Pages (from-to) | 355-363 |
Number of pages | 9 |
Journal | Chemical Engineering and Technology |
Volume | 32 |
Issue number | 3 |
DOIs | |
Publication status | Published - 2009 |
MoE publication type | A1 Journal article-refereed |
Keywords
- Carbon capture
- Circulating fluidized beds
- Modeling
- Oxy-fuel combustion
- Pilot testing