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Biomass Combined Heat and Power Catalog of Technologies

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Biomass Combined Heat and Power Catalog of Technologies ( biomass-combined-heat-and-power-catalog-technologies )

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EPA Combined Heat and Power Partnership Biomass CHP Catalog Table 5-9. Comparison of Fixed Bed Gasification Technologies Type of Gasifier Downdraft Updraft Crossflow Operation Biomass is introduced from the top and moves downward. Oxidizer (air) is introduced at the top and flows downward. Syngas is extracted at the bottom at grate level. Biomass is introduced from the top and moves downward. Oxidizer is introduced at the bottom and flows upward. Some drying occurs. Syngas is extracted at the top. Biomass is introduced from the top and moves downward. Oxidizer is introduced at the bottom and flows across the bed. Syngas is extracted opposite the air nozzle at the grate. Advantages Tars and particulate in the syngas are lower, allowing direct use in some engines without cleanup. The grate is not exposed to high temperatures. Can handle higher-moisture biomass. Higher temperatures can destroy some toxins and slag minerals and metal. Higher tar content adds to heating value. Simplest of designs. Stronger circulation in the hot zone. Lower temperatures allow the use of less expensive construction materials. Disadvantages Biomass must be very dry (<20 percent moisture content). The syngas is hot and must be cooled if compression or extensive cleanup is required. About 4 to 7 percent of the carbon is unconverted and remains in the ash. Higher tar content can foul engines or compressors. The grate is exposed to high temperatures and must be cooled or otherwise protected. More complicated to operate. Reported issues with slagging. High levels of carbon (33%) in the ash. Table 5-10. Typical Characteristics of a Fixed Bed Gasifier Fuel size (inches) Fuel ash content (% weight) Operating temperature (°F) Control Turn-down ratio Construction material Capacity (MWthermal) (tons biomass/day) Start-up time Operator attention Tar content (lb/MMBtu product gas) Heating value (Btu/scf) HHV Source: GasNet, n.d. 0.4-4 <6 1450-2550 Simple 4:1 Mild steel + refractory <5 (<30) Minutes Low <1.2 130 Parameter Fixed Bed, Downdraft 5. Biomass Conversion Technologies 48

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