Page 183 - Biomass Gasification, Pyrolysis And Torrefaction Practical Design and Theory
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160                          Biomass Gasification, Pyrolysis and Torrefaction


                     90                        40
                     80                        38
                     70                        36
                                               34          “Solid char”
                     60                        32
                    Yield (%)  50              30  Heating value (Mj/kg)  Gases (non
                                                           condensable)
                     40
                     30                        28          “Heating value
                                                           of char”
                                               26
                     20
                                               24
                     10                        22
                      0                        20
                      200   400  600   800  1000
                             Temperature (°C)
            FIGURE 5.8 Char yield from pyrolysis decreases with temperature while gas yield increases.
            Heating value of the solid char produced increases with temperature. Source: Data for grape
            bagasse (0.63 1.0 mm and HHV 17.2 MJ/kg dry) replotted from Encinar et al. (1996).

               The heating rate alone, however, does not define the product. The resi-
            dence time of the product in the reactor is also important. During slow heating,
            a slow or gradual removal of volatiles from the reactor permits a secondary
            reaction to occur between char particles and volatiles, leading to a secondary
            char formation.
               The operating parameters of a pyrolyzer are adjusted to meet the require-
            ment of the final product of interest. Tentative design norms for heating in a
            pyrolyzer include the following:
            a. To maximize char production, use a slow heating rate (,0.01 2.0 C/s),

               a low final temperature, and a long gas residence time.
            b. To maximize liquid yield, use a high heating rate, a moderate final
               temperature (450 600 C), and a short gas residence time.

            c. To maximize gas production, use a moderate to slow heating rate, a high
               final temperature (700 900 C), and a long gas residence time.

               Production of charcoal through carbonization uses step (a). Fast pyrolysis
            uses step (b) to maximize liquid yield. Step (c) is used when gas production
            is to be maximized.


            5.3.4 Effect of Particle Size
            The composition, size, shape, and physical structure of the biomass could
            exert some influence on the pyrolysis product through their effect on heating
            rate. Finer biomass particles offer less resistance to the escape of condens-
            able gases, which therefore escape relatively easily to the surroundings
            before undergoing secondary cracking. This results in a higher liquid yield.
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