Steam-bubbling fluidized bed (BFB) gasification offers a carbon-efficient route for coupling solid-waste valorization with microbial upgrading. This work investigates the pilot-scale production of a CO-lean, H₂/CO₂-rich syngas tailored for fermentation applications, by gasifying industrial waste wood and hydrochar in a dual-zone bubbling fluidized-bed reactor. A design-of-experiments framework varied bed temperature (350–550 °C), freeboard temperature (740–860 °C), air equivalence ratio (6–40 %), and steam-to-biomass ratio (0–1 kg/kg). Real-time gas analysis quantified product gas composition, while process performance was assessed via cold-gas efficiency (CGE), gas composition and lower heating value (LHV).
Optimal conditions for waste wood (freeboard 860 °C, steam = 1 kg/kg) yielded 21 vol.% H₂, 17 vol.% CO₂, 13 vol.% CO and CGE = 82.6 %. Hydrochar delivered 37 vol.% H₂,17 vol.% CO₂, 14 vol.% CO and CGE = 86.01 %, at lower bed temperatures (∼350 °C). Unlike previous gasification studies primarily focused on maximizing hydrogen yield or syngas heating value, this work targets fermentation-grade syngas compositions optimized for microbial conversion, demonstrating that feedstock selection and steam dosing are critical levers for controlling H₂/CO₂ ratios and minimizing CO inhibition.
These results constitute an innovative pilot-scale comparison of waste wood and HTC hydrochar gasification, highlighting a novel approach to tailoring syngas composition for biological upgrading and providing a validated process blueprint for integrating thermochemical conversion with CO₂ utilisation, advancing the objectives of sustainable chemistry for climate-action technologies.
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