Page 298 - Biomass Gasification, Pyrolysis And Torrefaction Practical Design and Theory
P. 298

274                          Biomass Gasification, Pyrolysis and Torrefaction



                                        Biomass inc






                                                            Raw syngas








                                                     Air or oxygen feed




                   Plasma torch


                                                Slag
            FIGURE 8.19 Plasma gasification of solid waste.



            it, is much lower (2700 4500 C). The downstream temperature is still suffi-
            ciently high, however, to pyrolyze complex hydrocarbons into simple gases
            such as CO and H 2 . Simultaneously, all inorganic components (e.g., glass,
            metals, silicates, and heavy metals) are fused into a volcanic-type lava,
            which after cooling forms an inert basaltic slag. The product gas leaves the
            gasifier at very high temperatures (1000 1200 C).

               A typical plasma reactor provides exceptionally high temperature that
            cause the tar products to be cracked and harmful products like dioxin and
            furan to be destroyed.
               Owing to the high reactor temperature and the presence of chlorine in
            wastes, the life of the reactor liner is an issue. However, an attractive feature
            is that plasma gasification is relatively insensitive to the quality of the feed-
            stock. This is the result of an independent energy source run by electricity
            instead of partial combustion of the gasification product.



            8.6 PROCESS DESIGN
            The design of a gasifier involves both process and hardware. The process
            design gives the type and yield of the product, operating conditions, and
            the basic size of the reactor. The hardware design involves structural
   293   294   295   296   297   298   299   300   301   302   303