Characteristics and kinetics of biomass tar cracking in a micro fluidized bed
Abstract
This study is devoted to investigate the characteristics and kinetics of biomass tar cracking in a micro fluidized bed reactor for liquids (MFBRL). The carbon balance and conversion were measured to estimate the performance of MFBRL, and the results showed good reproducibility and reliability. H2, CH4 and CO comprised the vast bulk of the producer gas and the total volume fraction of them increased from 69.85% to 93.62% (973–1173 K). Kinetic parameters, including reaction order, pre-exponential factor and apparent activation energy, were studied with the isothermal method. The reaction orders varied greatly with temperature, suggesting that temperature significantly affected the reaction mechanism. The pre-exponential factors for H2, CH4, CO and gas mixtures were in the range of 2.37 × 103 to 2.87 × 105 S−1, while the apparent activation energies ranged from 62.96–100.2 kJ mol−1. Compared to the fixed bed experiments, the derived results were obviously higher, indicating the kinetic parameters were more suitable for describing the intrinsic reactions.