4.7 Article

Modelling fuel flexibility in fixed-bed biomass conversion with a low primary air ratio in an updraft configuration

Journal

FUEL
Volume 296, Issue -, Pages -

Publisher

ELSEVIER SCI LTD
DOI: 10.1016/j.fuel.2021.120687

Keywords

Fixed-bed; Model; Updraft; Counter-current; Biomass gasification; Biomass combustion

Funding

  1. Austrian Federal Government's Climate and Energy Fund (Klimaund Energiefonds) [858771]
  2. European Union's Horizon 2020 Research and Innovation Programme [818012]
  3. H2020 Societal Challenges Programme [818012] Funding Source: H2020 Societal Challenges Programme

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Fixed-bed biomass conversion with low primary air ratio and counter-current configuration shows potential for emission reduction and high feedstock flexibility. The validated 1D bed model accurately predicts temperatures and gas composition, while also investigating fuel flexibility in different scenarios.
Fixed-bed biomass conversion with a low primary air ratio and a counter-current configuration has a high feedstock flexibility, as it resembles updraft gasification, and the potential to reduce emissions when integrated in biomass combustion systems. A 1D bed model was validated with experimental results from a biomass combustion boiler with such a bed conversion system, predicting with a good accuracy the temperatures in the reactor and producer gas composition. The model was applied for different cases to investigate the fuel flexibility of this combustion system, including the influence of moisture content and the maximum temperatures achieved in the bed. It was shown that with variations in fuel moisture content from 8 to 30% mass w.b. the producer gas composition, char reduction to CO or maximum temperatures at the grate were not affected due to the separation of the char conversion and pyrolysis/drying zones. Flue gas recirculation was the only possible measure with the tested configuration to reduce the maximum temperatures close to the grate, which is beneficial e.g. to avoid slagging with complicated fuels. A higher tar content was obtained than in conventional updraft gasifiers, which is attributed to the absence of tar condensation in the bed due to the limited height of the reactor and the integration in the combustion chamber. The presented model can support the development of such combustion technologies and is a relevant basis for detailed CFD simulations of the bed or gas phase conversion.

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