Page 301 - Biomass Gasification, Pyrolysis And Torrefaction Practical Design and Theory
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Chapter | 8  Design of Biomass Gasifiers                     277


             basis. By using the definition of these, one can relate the HHV on moisture-
             ash-free basis to that on only dry-basis value as:


                                                 1 2 M
                              HHV daf 5 HHV d                           (8.8)
                                              1 2 ASH 2 M
             where the subscripts d and daf refer to dry and moisture-ash-free basis,
             respectively; M is the moisture fraction; and ASH is the ash fraction in fuel
             on a raw-fuel basis.
                On a dry basis, HHV d is typically in the range 18 21 MJ/kg (Van Loo and
             Koppejan, 2003, p. 48). It may be calculated from the ultimate analysis for the
             biomass using the following equation (Van Loo and Koppejan, 2003, p. 29):
                        HHV d 5 0:3491C 1 1:1783H 1 0:1005S 2 0:0151N
                                                                        (8.9)
                               2 0:1034O 2 0:0211ASH
             where C, H, S, N, O, and ASH are the mass fraction of carbon, hydrogen,
             sulfur, nitrogen, oxygen, and ash in the fuel on a dry basis.

             8.6.2.3 Flow-Rate of Gasifying Medium
             The amount of gasification medium has a major influence on yield and com-
             position of the product gas. This section discusses methods for choosing
             that amount.


             Air
             The theoretical air requirement for complete combustion of a unit mass of a
             fuel, m th , is an important parameter. It is known as the stoichiometric air
             requirement. Its calculation is shown in Eq. (3.32). For an air-blown gasifier
             operating, the amount of air required, M a , for gasification of unit mass of bio-
             mass is found by multiplying it by another parameter equivalence ratio (ER):

                                       M a 5 m th ER                   (8.10)
                For a fuel feed rate of M f , the air requirement of the gasifier, M fa , is:
                                                                       (8.11)
                                     M fa 5 m th ER 3 M f
                For a biomass gasifier, 0.25 may be taken as a first-guess value for ER.
             A more detailed discussion of this is presented next.

             8.6.2.4 Equivalence Ratio
             Equivalence ratio (ER) is an important design parameter for a gasifier. It is
             the ratio of the actual air fuel ratio to the stoichiometric air fuel ratio. This
             definition is the same as that of excess air (EA) used for a combustion sys-
             tem, except that it is used only for air-deficient situations, such as those
             found in a gasifier.
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