Page 290 - Biomass Gasification, Pyrolysis And Torrefaction Practical Design and Theory
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266                          Biomass Gasification, Pyrolysis and Torrefaction


                              Upflowing      Downflowing
                              chamber         chamber














                               Fluidizing agents

            FIGURE 8.13 Internally circulating dual fluidized-bed gasifier.



            and connected by a window at the bottom of the division wall separating
            them. The chambers are fluidized at different velocities (Figure 8.13), which
            result in their having varying bed densities. As the bed height is the same in
            both, the hydrostatic pressure at the bottom of the two chambers is different.
            The biomass and sand, thus, flow from the higher-density chamber to the
            lower-density chamber, creating a continuous circulation of bed materials
            similar to the natural circulation in a boiler. This helps increase the residence
            time of solids in the fluidized bed.
               Such an arrangement can provide a more uniform distribution of biomass
            particles in the reactor, with increased gasification yield and decreased tar
            and fine solids (char) in the syngas (Freda et al., 2008). A special feature of
            the twin reactor is that more air or oxygen can be added in one part of the
            bed to encourage combustion, and more steam can be added in another part
            to encourage gasification.

            8.3.2.3 Chemical Looping Gasifier
            Primary motivation of chemical looping gasification is production of two
            separate streams of gases—a product gas rich in hydrogen and a gas stream
            rich in carbon dioxide (CO 2 ) such that the latter can be sequestrated while
            the hydrogen can be used for applications that require hydrogen-rich gas.
            The system uses calcium oxide as a carrier of carbon dioxide between two
            reactors: a gasifier (bubbling fluidized bed) and a regenerator (CFB). The
            CO 2 produced during gasification is captured by the CaO and released in a
            second reactor during sorbent regeneration.
               Figure 8.14 is a schematic of the chemical looping process. Biomass is
            fed into the gasifier that receives calcium oxide from the regenerator and
            superheated steam from an external source. During gasification, the CO 2
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