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This thesis develops a circulating fluidized bed reactor model for biomass fast pyrolysis process simulation. The model incorporates a flexible pyrolysis reaction mechanism, one-dimensional steady-state momentum and energy equations, and accounts for the catalytic effect of biomass alkali metals on product yields. Simulation results for product yields are validated against experimental data. Fluid dynamics results are verified against a two-dimensional reactor model. Model assumptions regarding biomass part

Author

Candra

Language

EN