Abstract
A steady state simulation approach for the simulation of
circulating fluidized bed furnaces is presented in the
paper. The feasibility of the method is studied by
applying it on coal combustion in the circulating
fluidized bed combustor at Chalmers University of
Technology. In addition to hydrodynamics, a steady-state
description of heat transfer and chemistry, including
homogeneous and heterogeneous reactions, is included in
the modeling. Fuel particles are modeled applying the
Lagrangian particle tracking method. The obtained
simulation results are comparable with the ones presented
in the literature. The study proves the steady state
modeling approach to be feasible
Original language | English |
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Title of host publication | 21st International Conference on Fluidized Bed Combustion Proceedings Volume 2 |
Place of Publication | Napoli, Italia |
Pages | 891-898 |
Publication status | Published - 2012 |
MoE publication type | A4 Article in a conference publication |
Event | 21st International Conference on Fluidized Bed Combustion, 21FBC - Napoli, Italy Duration: 3 Jun 2012 → 6 Jun 2012 |
Conference
Conference | 21st International Conference on Fluidized Bed Combustion, 21FBC |
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Abbreviated title | 21FBC |
Country/Territory | Italy |
City | Napoli |
Period | 3/06/12 → 6/06/12 |
Keywords
- Circulating fluidized bed
- CFD
- time averaged
- combustion
- modeling