Page 262 - Biosystems Engineering
P. 262

240    Cha pte r  Se v e n

               the gasoline range. The results obtained by Piskorz et al. (1989) are
               very interesting because it proved the feasibility of hydrotreating
               decanted oils. In fact, the oils obtained from the slow pyrolysis reac-
               tors and by high-pressure liquefaction are also decanted oils with
               relatively low contents of polar compounds and tend to behave satis-
               factorily during hydrotreatment. New hydrotreatment studies with
               pyrolytic lignin (decanted oil) were carried out in 2005 by UOP LLC,
               a Honeywell company, and Pacific Northwest National Laboratory
               (PNNL) (Marinangeli et al. 2005). Two catalysts were tested. Although
               PNNL used Pd on a carbon catalyst in a continuous pilot plant, UOP
               used a Ni–Mo catalyst in a batch autoclave. The results obtained were
               very similar to those obtained by Piskorz et al. (1989). The yield of
               upgraded oils varies between 40 and 55 percent with an oxygen
               removal of 69 to 93 percent. Between 30 and 60 percent of the bio-oil
               was converted to naphtha.
                   UOP, PNNL, and NREL have recently shown (Holmgren et al.
               2008) that although it is more difficult, the hydrotreatment of whole
               bio-oils is also viable. There was 21 mass% of the oil converted to
               distillable products with boiling points similar to naphtha and
               another 21 percent was converted to compounds with boiling points
               similar to diesel. The rest of the bio-oil was converted to CO , water,
                                                                  2
               and light hydrocarbons. Thus, around 28 mass% of the biomass can
               be converted into fungible transportation fuel. These values are very
               high if we take into account that current efforts at enzymatic hydro-
               lysis only aim at producing 63.2 gallons of ethanol per ton of biomass
               processed. The fast pyrolysis/hydrotreatment pathway could yield
               148 gallons of ethanol equivalent per ton of biomass. Recent economic
               analyses performed by UOP (Marinangeli et al. 2005) suggest that the
               hydrotreatment of a bio-oil water-insoluble fraction is economically
               viable at petroleum prices over $50 per barrel. Although hydrotreat-
               ment of fast pyrolysis oils still requires more development to enable
               large commercial operations, it is certainly one of the most promising
               alternatives to convert biomass into transportation fuels.



          7.7 Bio-Oil Refineries
               The use of concepts like bio-based economy and biorefineries is not new,
               but their importance has only been recognized recently. It is now gen-
               erally accepted that biomass-derived products will have better oppor-
               tunities to compete with our dominant petroleum economy.
                   The equilibrium between the cost of transportation and savings
               associated with the economies of scale will determine the feasibility
               of building centralized refineries near consumer centers, or distrib-
               uted rural refineries closer to the biomass resources. The main goal of
               a biorefinery is to produce high-value low-volume (HVLV) and low-
               value high-volume (LVHV) marketable products at competitive cost
   257   258   259   260   261   262   263   264   265   266   267