Page 241 - Synthetic Fuels Handbook
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FUELS FROM BIOMASS                    227

             Underutilized wood species include Southern red oak, poplar, and various small diameter
             hardwood species. Unharvested dead and diseased trees can comprise a major resource in
             some regions. When such timber has accumulated in abundance, it comprises a fire hazard
             and must be removed. Such low grade wood generally has little value and is often removed
             by prescribed burns in order to reduce the risk of wildfires.
               Waste streams can also be exploited for ethanol production. They are often inexpensive
             to obtain, and in many instances they have a negative value attributable to current disposal
             costs. Some principal waste streams currently under consideration include mixed paper from
             municipal solid waste, cellulosic fiber fines from recycled paper mills, bagasse from sugar
             manufacture, corn fiber, potato waste, and citrus waste, sulfite waste liquors, and hydrolysis
             streams from fiber board manufacture. Each waste stream has its own unique characteristics,
             and they generally vary from one source or time to another. Waste streams with lower lignin
             contents and smaller particle sizes are easier to deal with than those with higher lignin con-
             tents and larger particle sizes. Waste paper that has been treated by a chemical pulping process
             is much more readily converted than is native wood or herbaceous residue.


             8.1.2 Feedstock Properties
             The components of biomass include cellulose, hemicelluloses, lignin, lipids, proteins,
             simple sugars, starches, water, hydrocarbons, ash-forming constituents, and extractable
             compounds. These constituents influence the properties of biomass and, in turn, have a
             significant bearing on the thermal conversion of biomass. In addition, the high moisture,
             oxygen content, hydrogen content, and volatile matter content, and low energy density also
             influence biomass conversion.
               The high oxygen and hydrogen contents account for the high proportion of volatile mat-
             ter and consequent high yields of gases and liquids on pyrolysis. A relatively high water
             yield results from the high oxygen concentration in biomass, and which consumes con-
             siderable hydrogen. Consequently the advantages of the high hydrogen-to-carbon (H/C)
             ratio associated with biomass are not reflected in the products to the extent that might be
             expected. In fact, pyrolysis gases can be deficient in pure hydrogen and pyrolysis liquids
             are highly oxygenated, viscous tars.
               An additional and significant source of water vapor in biomass gases is the high mois-
             ture content of the source materials. In countercurrent flow schemes such as the Lurgi
             moving bed gasifier, this water is evolved in the relatively low temperature drying and
             pyrolysis zones and does not partake in gas phase or carbon-steam gasification reactions.
             On the other hand, in fluidized bed systems the moisture is evolved in the high temperature
             well-mixed reaction zone and therefore does participate in the reactions. If the system is
             directly heated and air blown, the additional heat required to evaporate the water will result
             in more nitrogen being introduced, and more carbon dioxide being produced, reducing the
             calorific value of the product gas. As the gas from air-blown processes is, in any case, a low-
             calorific value product, this factor is probably of little consequence other than with very wet
             feedstock. In oxygen-blown systems, however, the additional pure oxygen is required and
             higher carbon dioxide content of the medium calorific value off-gas may be of sufficient
             impact to dictate some degree of drying as a pretreatment.
               Apart from drying, additional beneficiation may be undertaken to yield a resource of
             higher energy density. These operations will normally be undertaken at the source, so trans-
             port and subsequent storage costs may be reduced as well. Beneficiation steps include size
             reduction and densification. Waste heat, if available, may be used for drying, while size
             reduction and compression to form pellets or briquettes is estimated to require less than
             2 percent of the energy in the dry biomass. Nevertheless, these operations are time consum-
             ing, and can be either labor or capital intensive.
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