Biomass gasification in an autothermal semi-industrial fluidized bed gasifier: Syngas characterization and energy balance
Peter Badu, Matthieu Debal, Pierre Girods, S. Aubert, Yann Rogaume
Abstract
Biomass gasification is well-established in industrial applications, but semi-industrial autothermal systems remain underexplored despite their role as a bridge between laboratory scale and full-scale deployment. Understanding syngas characteristics, energy recovery, and system efficiency at this scale is critical for optimizing industrial gasification. This study examines air gasification of woody biomass in a 200 kW autothermal bubbling fluidized bed gasifier operating at equivalence ratios (ER) 0.22–0.45 with recorded bed temperatures of 695–860 °C. Key performance indicators, including syngas composition, lower heating values (LHV), cold gas efficiency (CGE), carbon conversion efficiency (CCE), and energy distribution of the near-industrial system, were analyzed. Results show syngas primarily contained H 2 (6.4–11.3 %), CO (8.5–16.6 %), CH 4 (3.0–5.5 %), and CO 2 (15.6–19.4 %), with LHV of 3.9–7.1 MJ/Nm 3 . CGE reached 51.8–71.4 %, and CCE 78.6–98.5 %. Overall system efficiency (79–93 %) highlights the role of energy recovery from syngas cooling and gathered solid residues in improving large-scale gasification viability. This study provides novel insights into optimizing semi-industrial gasification, demonstrating the feasibility of integrated energy recovery for enhanced efficiency and sustainability. • High gasification efficiency achieved: 79–93 % with energy recovery from syngas cooling and solid residues. • Gasifier bed temperatures are maintained solely by heat from exothermic reactions. • Lower heating value of syngas ranged from 3.9 to 7.1 MJ/Nm 3 for all biomasses. • Cold gas efficiency improved with higher equivalence ratios, up to 71.4 %.