Page 248 - Biomass Gasification, Pyrolysis And Torrefaction Practical Design and Theory
P. 248

224                          Biomass Gasification, Pyrolysis and Torrefaction



              TABLE 7.6 Activation Energy and Preexponential Factors for Birch Char
              Using the Langmuir Hinshelwood Rate Constants for CO 2 Gasification
              Langmuir Hinshelwood Rate  Activation Energy  Preexponential Factor
                                                               21
                            21
              Constants (s 21  bar )     E (kJ/mol)     A (s 21  bar )
                                         165            1.3 3 10 5
              k b1
                                         20.8           0.36
              k b2
              k b3                       236            3.23 3 10 7
              Source: Adapted from Barrio and Hustad (2001).






              TABLE 7.7 Typical Values for Activation Energy, Preexponential Factor,
              and Reaction Order for Char in the Boudouard Reaction

                     Activation                     Reaction
              Char   Energy E     Preexponential    Order,
                                              21
              Origin  (kJ/mol)    Factor A (s 21  bar )  n (2)  References
                                         6 21
              Birch  215            3.1 3 10 s  bar 20.38  0.38  Barrio and
                                                              Hustad (2001)
              Dry    109.5        153.5 s 21  bar 21  1.2     Barrio and
              poplar                                          Hustad (2001)
                                          8 21
              Cotton  196           4.85 3 10 s     0.6       DeGroot and
              wood                                            Shafizadeh
                                                              (1984)
                                          8 21
              Douglas  221         19.67 3 10 s     0.6       DeGroot and
              fir                                             Shafizadeh
                                                              (1984)
                                          6 21
              Wheat  205.6          5.81 3 10 s     0.59      Risnes et al.
              straw                                           (2001)
                                          6 21
              Spruce  220          21.16 3 10 s     0.36      Risnes et al.
                                                              (2001)





                                2CO-CO 2 1 C2172 kJ=mol               (7.45)
               The preceding reaction becomes thermodynamically feasible when
            (P 2 CO  =P CO 2 ) is much greater than that of the equilibrium constant of the
            Boudouard reaction (Littlewood, 1977).
   243   244   245   246   247   248   249   250   251   252   253