Page 177 - Advanced Gas Turbine Cycles
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Chapter 8. Novel gas mrbine cycles            I43

       carbon monoxide, is
                           1
            [ AH1 SyN =P[AHH~ T +( 1 - a)[AHc& 1~+(4a- P)[Affcol~= [AHIcH~ + [AHITcR,
       This is thus greater than the heating value of the original unit mole of methane supplied but
       is contained in a larger number of moles of syngas (N).


       8.5.3. Partial oxidation

         In the second chemical reaction to be considered, insufficient oxygen is supplied to the
       fuel for stoichiometric combustion (50%), but steam is also supplied (Fig. 8.5~). Now the
       chemical reactions involved in the partial combustion are:
            A :  CH4 + H20 * CO + 3H2,
       the steam reforming reaction;
            B:  CO+H20*C02+HZ,

       the water shift reaction; and
            C : CH, + 0.502 H CO + 2H2,
       the PO reaction.
         As in the steam/TCR analysis the Boudouard reaction is ignored here, together with
       direct methane decomposition.
         The PO reaction, leading to five constituents, is now
            2CH4 + $2  + nH20

              =+(I  -y)CH4+6C02+(y-6+1)CO+(3y+6+2)H2+(n-             y-6)H20
       The solution then follows along the same lines as for TCR; if the temperature and pressure
       are  known  then  y,  6  and  the  resulting  mole  fractions  can  be  determined  from  the
       equilibrium constants. The temperature change between inlet and outlet is now likely to be
       higher than in the TCR reactions, so the determination of the Kps as functions of a single
       mean temperature for the reaction is more difficult.


       8.5.4.  Thermo-chemical recuperation using flue gases @ue gas/TCR)

         Another approach which has been suggested for thenno-chemical reforming can now
       be  considered. It involves recirculation of exhaust gas from the turbine, which already
       contains some C02 and H20, to mix with the fuel in a reformer; the resulting syngas is then
       supplied to the main combustion chamber. The combustion process producing the flue gas
       is assumed to be virtually stoichiometric, with a small amount of excess air. The flue gas
       thus contains a small amount of oxygen and Po of the fuel (CH4) may take place, together
       with the steam reforming and water shift reactions.
         The ‘Van’t Hoff box’ for this process will produce five components+arbon  dioxide,
       carbon  monoxide,  water  vapour  and  hydrogen,  and  unconverted  methane.  Again  if
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