The invention discloses a gasification and high-temperature
tar removal and dust removal
integrated technology of a
biomass circulating
fluidized bed.
Biomass particles which are smaller than 5 mm andsupplemented heat carriers enter the bottom of the circulating
fluidized bed,
pyrolysis,
combustion and gasification reactions occur at the temperature of 750-900 DEG C, and residual semi-
coke and heat carriers are carried at high speed, go upward along with synthesized gas to reach the top of the circulating
fluidized bed, and then are subjected to four-stage gas-
solid separation; in the first stage of separation, the large-particle carriers and the semi-
coke are used as a
fuel gas pyrolysis catalyst and a filtering material for filtering and dust removing, enter a movable
bed filter device,and then return to a turbulence fluidized
bed for a gasification reaction after super-thin dust is separated out, and the super-thin dust is delivered out as
silicon-
potassium products; in the secondstage of separation, the medium-
small particle carriers and the semi-
coke are directly circulated back to the turbulence fluidized
bed, in the third stage of separation, fine particles are dischargedas
silicon-
potassium products, in the fourth stage, the movable bed filter device conducts secondary
catalytic pyrolysis on a small amount of
tar in
fuel gas at the temperature of 700-850 DEG C through synergism of the high-temperature carriers and semi-coke to obtain
methane,
ethylene and others, meanwhile, the super-thin dust is removed, and purified
fuel gas is delivered out as products.