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Biomass Pyr olysis and Bio-Oil Refineries     219


                         H           O
                 HO              O                         C=C  CH-CH
                          O CH 3     CH + H O + CO + CO            O
                                                2
                                          2
                                                      R  O
                                                                   6
                      Fragmentation        Fragmentation
                            3                   3                    Char
                  1                    2             O
                                                   HO
                 Fast             Depolymerization      H + ..  5
           Cellulose  Cellulose of low        H   O
                    DP (active cellulose)      H          H
                                                     H
                                                 HO   HO
                                 Alkali cation–inhibited   Lignin-inhibited
                                     mechanism             mechanism
                          7                        4
                   (Slow pyrolysis)   Acid (phosphoric acids) +   H O
                                         water catalyzed      2     O
                                                       O
                  H O + CO  + CO + chain linked       O          O  CH
                   2
                         2
                        by ether groups
                                             Levoglucosenone  O
          FIGURE 7.7  Cellulose thermochemical-degradation reactions (Garcia-Pérez and
          Metcalf 2008).

               Piskorz et al. 1986; Kim et al. 2001; Wooten et al. 2004; Mamleev et al.
               2007; Zickler et al. 2007); (2) depolymerization of active cellulose to
               produce mono- and oligosugars (Radlein 1987; Radlein et al. 1991a,
               1991b; Piskorz et al. 2000); (3) fragmentation or open-ring reactions
               controlled by the presence of alkalines (Broido and Kilzer 1963;
               Radlein et al. 1991a, 1991b; Piskorz et al. 1986, 1989a, 1989b, 2000;
               Arisz et al. 1990; Lomax et al. 1991; Julien et al. 1993; Evans and Milne
               1987a, 1987b; Richards 1987); (4) acid-catalyzed dehydratation reac-
               tions (Radlein et al. 1991a, 1991b; Dobele et al. 2001, 2003; Kawamoto
               et al. 2003a, 2003b, 2007a; Kawamoto and Saka 2006); (5) polymeriza-
               tion of anhydrosugars (Wooten et al. 2004; Hosoya et al. 2006, 2007a,
               1997b); (6) cross-linking reactions of fragmentation products to produce
               char; and (7) cross-linking reactions with evolution of water, which is
               typical of slow heating rate regimes (Kilzer and Broido 1965).
                   Low heating rates tend to favor the cross-linking reactions leading
               to the formation of larger yields of char and water [see reaction (7),
               Fig. 7.7]. Conversely, high heating rates will favor depolymerization
               reactions resulting in higher bio-oil yields.

               Hemicellulose
               Xylan thermal-degradation reactions follow a similar pathway to the
               one described for cellulose. Xylan possesses ion-exchange sites, which
               make it particularly susceptible to the uptake of impurity cations. The
               main products of the thermal decomposition of hemicelluloses found
               in the bio-oils are acetic acid, furans, and mono- and oligopentoses.
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