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Chapter 1 Biomass and technologies for its exploitation As shown in Figure 1.19, biomass dust and the oxidiser (normally oxygen) are introduced, together with the portion of charcoal recirculated from the cyclone, in the bottom part of the reactor, where the combustion takes place. Its products go up passing through a diffuser, that reduces their velocity, and enter the second stage, that is the reduction zone, where additional biomass is fed. Since the solid fuel is present in dust form, contact surfaces are very high and hence reaction times are very short. The process happens at very high temperature (and normally at high pressure, in this case also allowing a coupling with GTs) so that firstly the syngas results completely free from tars (that are in vapour form) and secondly ash melts, being then collected on the bottom of the reactor in the form of slag. On the other hand, high temperature causes low thermal efficiencies and syngas must be cooled after leaving the gasifier. Moreover, these devices are often cooled by means of boiling water jackets and the produced vapour can be used in the process or in other applications [1.31]. Figure 1.19 – Scheme of a circulating entrained bed gasifier. 48PDF Image | SMALL-SCALE BIOMASS POWER GENERATION
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