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258                          Biomass Gasification, Pyrolysis and Torrefaction


               Throated downdraft gasifiers are not suitable for scale-up to larger sizes
            because they do not allow for uniform distribution of flow and temperature
            in the constricted area. To above 1 MW th capacity, an annular constriction
            can be employed, but this has not been the practice to date.


            8.2.3 Crossdraft Gasifiers

            A crossdraft gasifier is a cocurrent moving-bed reactor, in which the fuel is
            fed from the top and air is injected through a nozzle from the side
            (Figure 8.7) of the gasifier. It is primarily used for gasification of charcoal
            with very low ash content. Unlike the downdraft and updraft types, it
            releases the product from its sidewall opposite to the entry point of the air
            for gasification. Because of this configuration, the design is also referred to
            as sidedraft. High-velocity air enters the gasifier through a nozzle set at a
            certain height above the grate. Excess oxygen in front of the nozzles facili-
            tates combustion (oxidation) of part of the char, creating a very-high-

            temperature (.1500 C) zone. The remaining char is then gasified to CO
            downstream in the next zone (Figure 8.7). The product gas exits from the
            opposite side of the gasifier. Heat from the combustion zone is conducted
            around the pyrolysis zone, so the fresh biomass is pyrolyzed while passing
            through it.
               This type of gasifier is generally used in small-scale biomass units. One
            of its important features is a relatively small reaction zone with low thermal
            capacity, which gives a faster response time than that of any other moving-
            bed type. Moreover, start-up time (5 10 min) is much shorter than in down-
            draft and updraft units. These features allow a sidedraft gasifier to respond
            well to load changes when used directly to run an engine. Because its tar
                                        3
            production is low (0.01 0.1 g/nm ), a crossdraft gasifier requires a relatively
            simple gas-cleaning system.

                                         Biomass




                                         Drying
                                                    Gasification
                                          Pyrolysis
                           Combustion
                               Air                     Gas



                                   Ash
            FIGURE 8.7 Schematic of a crossdraft gasifier.
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