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Chapter 3 Working hypotheses and preliminary analysis In the new section dedicated to gasification, ThermoflexTM provides models for all these components: theoretically, a cleaning section downstream the gasifier could therefore be assembled. Nevertheless, it was mentioned in the previous pages that syngas exiting the gasifier is actually already clean, being composed only by CO, CO2, CH4, H2, H2O, N2 and Ar, apart from two sulphur compounds, i.e. H2S (hydrogen sulphide) and COS (carbonyl sulphide), moreover not having any effect in the following power section. Thus all models of devices dedicated to syngas cleaning are actually useless and are only meant to complete the plant model under a visual aspect, as they just introduce head losses and, in case of scrubbing or wet compression, determine a moisture variation (which is always completely being removed at the end of the treatment chain). Considering that these components often lead to computational problems, it is easy to understand why the final choice was to condensate the cleaning section into two simple components, i.e. a heat exchanger, simulating the temperature decrease (down to 25°C) and head losses along the process, and a moisture separator. Power consumption of the various real components have instead been charged to the gasifier. The resulting ThermoflexTM model is shown in Figure 3.13 (note the presence of the aftercooler, fed by a hypothetic water flow, yielding the aforementioned temperature decrease from 800°C to 500°C at the gasifier output). Temperature lowering Moisture separator Figure 3.13 – ThermoflexTM simplified gasification and syngas cleaning model. 107PDF Image | SMALL-SCALE BIOMASS POWER GENERATION
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