Page 247 - Synthetic Fuels Handbook
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FUELS FROM BIOMASS                    233

                Feedstock  Gas                  Feedstock




                                                              Drying zone
                                 Drying zone
                                                              Pyrolysis zone
                                 Pyrolysis zone               Hearth zone
                                 Reduction zone  Air          Air
                                                              Reduction zone
                                 Hearth zone                  Grats
                                 Grats
                                                             Gas
                  Air           Ash
                                                     Ash pit
                FIGURE 8.3  Updraft (left hand side) and downdraft (right hand side) fixed bed direct gasifiers.
                (Source:  Kavalov, B., and S. D. Peteves: “Status and Perspectives of Biomass-to-Liquid Fuels in
                the European Union,” European Commission. Directorate General Joint Research Centre (DG
                JRC). Institute for Energy, Petten, Netherlands, 2005.)

             and circulating (Fig. 8.4)—are not suitable for biomass-to-liquids production. In addition,
             downdraft fixed bed gasifiers face severe constraints in scaling and are fuel inflexible, being
             able to process only fuels with well-defined properties. Updraft fixed bed gasifiers have
             fewer restrictions in scaling but the produced gas contains a lot of tars and methane.
               Fluidized bed gasifiers generally do not encounter limitations in scaling and are more
             flexible concerning the particle size of fuels. Nevertheless, they still have limited fuel flex-
             ibility, due to a risk of slagging and fouling, agglomeration of bed material, and corrosion.
             The operating temperatures of air-blown fluidized bed gasifiers are therefore kept relatively
             low (800–1000°C), which implies incomplete decomposition of feedstocks, unless long
             residence times are used. Fluidized bed gasifiers (especially the bubbling bed ones) tend
             to contaminate the product gas with dust. The oxygen-blown atmospheric or pressurized


                                                   Gas + Inert + Char  Gas
                            Gas
                                                                    Cyclone

             Feedstock
                                  Gas phase
                                                                   Recycle
                                   reaction
                                           Feedstock               Fluidized bed
                                                                   gas phase
                                                                   reaction
                                   Bubbling
                                  fluidized bed

                 Grats                         Grats            Inert + Char
                                  Ash                          Ash
                         Air Air                       Air Air
             FIGURE 8.4  Bubbling (left hand side) and circulating (right hand side) fluidized bed direct gasifiers.
             (Source:  Kavalov, B., and S. D. Peteves: “Status and Perspectives of Biomass-to-Liquid Fuels in the
             European Union,” European Commission. Directorate General Joint Research Centre (DG JRC). Institute
             for Energy, Petten, Netherlands, 2005. )
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