Two phase modelling of Geldart B particles in a novel indirectly heated bubbling fluidized bed biomass steam reformer
نویسندگان
چکیده
This work focuses on the numerical modelling and experimental validation of hydrodynamic behaviour a novel 50 kWth indirectly heated bubbling fluidized bed steam reformer. The beds with immersed vertical tubes complex geometries in general have not been thoroughly investigated terms coupled for pilot scale reactors. Therefore, present study contributes to hydrodynamics field, while investigating reactor concept. Simulations were performed employing Two-Fluid Model approach, using Kinetic Theory Granular Flows (KTGF) adjusted Syamlal O’Brien drag model. reactor’s was simulated successfully, as showcased by comparison global metrics (bed height, pressure drop) between computational results. without considering an additional nitrogen gas feed side (feeding system pressurization). Overall, both cases, realistic values particle restitution coefficient channelling flow near walls observed. Larger bubbles appeared be forming outer wall no side-flow simulations. opposite encountered simulations due stream-like moving up against wall. choice limit 72° symmetry domain validated, indicating possibility further reduction. Finally, it argued that increasing diameter could potentially lead reduction observed fluidization media improve mixing achieved thus conversion efficiency IHBFBSR during gasification applications.
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ژورنال
عنوان ژورنال: Chemical Engineering Journal
سال: 2022
ISSN: ['1873-3212', '1385-8947']
DOI: https://doi.org/10.1016/j.cej.2022.135681