Page 131 - Handbook of Energy Engineering Calculations
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6. Compute the enthalpy of the products of the combustion process
               Enthalpy of the products of combustion, h  = m  (h               l600  – h ),  where  m   =
                                                                    p
                                                                           p
                                                                                                         p
                                                                                         77
               number of moles of the products; h         1600  = enthalpy of the products at 1600°F
               (871°C); h  = enthalpy of the products at 77°F (25°C). Thus, h  = (8 + 9 +
                            77
                                                                                              p
               189.2 + 37.5)(15,400 − 3750) = 2,839,100 Btu [6,259,100 Btu (SI)].

               7. Compute the air supply temperature at the combustion chamber inlet
               Since the combustion process is adiabatic, the enthalpy of the reactants h  =
                                                                                                         r
               h ,  where  h   =  (relative  weight  of  the  fuel  ×  its  heating  value)  +  [relative
                              r
                 p
               weight of the air × its specific heat × (air supply temperature − air source
               temperature)]. Therefore, h  = (114 × 19,100) + [(1600 + 5298) × 0.24 × (t  –
                                                r
                                                                                                         a
               77)]  +  2,839,100  Btu  [6,259,100  Btu  (SI)].  Solving  for  the  air  supply
               temperature, t  = [(2,839,100 − 2,177,400)/1655.5] + 77 = 477°F (247°C).
                                a


               Related Calculations. This procedure, appropriately modified, may be used
               to deal with similar questions involving such things as other fuels, different
               amounts of excess air, and variations in the condition(s) being sought under

               certain given circumstances.
                  The coefficient, (?) = 3.784 in step 2, is used to indicate that for each unit
               of  volume  of  oxygen,  O ,  12.5  in  this  case,  there  will  be  3.784  units  of
                                               2
               nitrogen,  N .  This  equates  to  an  approximate  composition  of  air  as  20.9
                              2
               percent oxygen and 79.1 percent “atmospheric nitrogen” (N ).  In  turn,  this
                                                                                          2
               creates  a  paradox,  because  page  200  of  Principles  of  Engineering
               Thermodynamics, by Kiefer et al., John Wiley & Sons, Inc., 1930, states air
               to be 20.99 percent oxygen and 79.01 percent atmospheric nitrogen, where

               the ratio N /O  = (?) = 79.01/20.99 = 3.764.
                            2
                                2
                  Also,  page  35  of  Applied  Energy  Conversion,  by  Skrotzki  and  Vopat,
               McGraw  Hill,  Inc.,  1945,  indicates  an  assumed  air  analysis  of  79  percent
               nitrogen and 21 percent oxygen, where (?) = 3.762. On that basis, a formula
               is  presented  for  the  amount  of  dry  air  chemically  necessary  for  complete
               combustion of a fuel consisting of atoms of carbon, hydrogen, and sulfur, or

               C, H, and S, respectively. That formula is W  = 11.5C + 34.5[H − (0/8)] +
                                                                       a
               4.32S, lb air/lb fuel (kg air/kg fuel).

                  The following derivation for the value of (?) should clear up the paradox
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