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EPA Combined Heat and Power Partnership Biomass CHP Catalog Fluidized Bed Gasifiers Fluidized bed gasifiers utilize the same gasification processes and offer higher performance than fixed bed systems, but with greater complexity and cost. Similar to fluidized bed boilers, the primary gasification process takes place in a bed of hot inert materials suspended by an upward motion of oxygen- deprived gas (Figure 5-7). As the amount of gas is augmented to achieve greater throughput, the bed will begin to levitate and become “fluidized.” Sand or alumina is often used to further improve the heat transfer. Notable benefits of fluidized bed devices are their high productivity (per area of bed) and flexibility. Fluidized bed gasifiers can also handle a wider range of biomass feedstocks with moisture contents up to 30 percent on average. Figure 5-7. Fluidized Bed Gasifier Source: Bain, 2006. There are three stages of fluidization that can occur on the gasifier depending on the design: bubbling, recirculating, and entrained flow. At the lower end of fluidization, the bed expands and begins to act as a fluid. As the velocity is increased, the bed will begin to “bubble.” With a further increase in airflow, the bed material begins to lift off the bed. This material is typically separated in a cyclone and “recirculated” to the bed. With still higher velocities, the bed material is entrained (i.e., picked up and carried off in the airflow). Fluidized bed gasifiers can be designed to use a portion of the pyrolysis gases to generate the heat to drive the process, or they can be externally fired. Operating the gasifier at higher pressures increases the throughput; however, this also increases the gasifier’s complexity and cost. In these units, the biomass is fully converted after going through the pyrolysis and char conversion processes. By reducing the quantity of air and process temperature, it is possible to operate fluidized bed boilers as gasifiers. In this operating mode, the gasifiers produce a gas with a heating value of slightly more than 100 Btu/cubic foot (ft3). This gas is burned above the bed as additional air supply is injected upstream of the boiler tube section. Table 5-11 provides typical physical characteristics of a fluidized bed gasifier. A number of advanced-concept fluidized bed gasifiers aiming to produce a syngas with a heating value between 250 and 400 Btu/ft3 are under development. This type of syngas would be more appropriate for use in gas 5. Biomass Conversion Technologies 49PDF Image | Biomass Combined Heat and Power Catalog of Technologies
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