Page 275 - Air pollution and greenhouse gases from basic concepts to engineering applications for air emission control
P. 275

8.4 Biofuels                                                    251

              In continuous operation, slurry feeding is a challenge because of the water
            evaporation at the end of the pipe. Poor conversions were reported because of the
            loss of water by condensation. Serious erosion and/or corrosion occurred on several
            spirals of the auger where the reaction was actually took place before the feedstock
            enters the reactor. Char formation was found to occur downstream because of lack
            of water brought about by back condensation. Some differences have been found in
            the chemical composition of the oil from the batch process and the semi-continuous
            process. A higher percentage of aromatic and/or unsaturated carbon was found in
            the oil produced using the semi-continuous process.



            8.4.4.2 Hydrothermal Liquefaction

            Hydrothermal liquefaction employs reactive hydrogen or carbon monoxide carrier
            gases to produce liquid fuel from organic matter at moderate temperatures. Tem-
            peratures between 300 and 400 °C correspond to the maximum yield of oil products
            [50]. Direct liquefaction involves rapid pyrolysis to produce liquids and/or organic
            vapors, whereas indirect liquefaction employs catalysts to convert non-condensable,
            gaseous products of pyrolysis, or gasification into liquid products.
              Technically, any matter with high organic content can be converted into another
            form by thermochemical conversion, but the conversion rate depends on the
            feedstock and the process itself. A variety of feedstocks are proven technically
            successful including high-carbon content materials such as coal, peat, and ligno-
            cellulosic material. Low-quality feedstock includes municipal and industrial wastes
            and agricultural residues. Studies on thermochemical conversion of biomass were
            predominantly focused on materials that are highly cellulosic, until recently an
            emerging interest in liquid waste such as livestock manure (e.g., [50]) and algae
            [34].
              Many factors affect the conversion rate of a HTC process. They include, but not
            limited to, temperature, pressure, retention time, reactant gases, feedstock, catalysts,
            if any, and the reactor design. These parameters were found to be most important as
            they dictate the yield and quality of the products. Regardless of the process, the new
            fuel is inevitably more expensive than its parent fuel due to the extra energy and
            equipment required for the conversion.
              Hydrothermal conversion is a process that is similar to cooking of food. The
            major differences between this process and other processes are use of wet feedstock
            as raw material because it saves energy from drying the feedstock. Also, the
            presence of water is beneficial for the conversion process.
              The primary reactions in the conversion of biomass to oil likely involve the
            formation of low-molar weight, water-soluble compounds such as glucose. Water
            also acts as solvent and alkaline catalysts. More importantly, water plays a critical
            role in the water-gas shift reaction
   270   271   272   273   274   275   276   277   278   279   280