Page 150 - Handbook of Energy Engineering Calculations
P. 150

(°C); other symbols as before. Using the values determined above, T  = [390
                                                                                                  lc
               − (0.855)(227)]/(l − 0.855) = 135l°F (732.8°C).


               2. Determine the system pinch/point and gas/steam profile
               Up to a gas inlet-temperature of approximately 1351°F (732.8°C), the pinch

               point can be arbitrarily selected. Beyond this, the feedwater inlet temperature
               limits  the  temperature  profile.  Let’s  then  select  a  pinch  point  of  25°F
               (13.9°C), Fig. 11. Then, T  the gas-turbine gas temperature at the pinch point,
                                               2
               °F (°C) = t  + pinch-point temperature difference, or 390°F + 25°F = 415°F
                             f
               (212.8°C).

                  Setting up an energy balance across the evaporator, assuming a heat loss of
               2 percent and a blow-down of 3 percent, leads to: Q             evap  = W  (1 − heat loss)
                                                                                         e
               (TEG  heat  capacity,  Btu/°F)  (T   −  T ),  where  W   =  TEG  flow,  lb/h;  heat
                                                                             e
                                                       1
                                                              2
               capacity  of  TEG  =  0.27  Btu/°F;  T   =  TEG  inlet  temperature,°F  (°C).
                                                              1
                                                                                                    6
               Substituting, Q    evap   =  150,000(0.98)(0.27)(950  −  415)  =  21.23  ×  10   Btu/h
               (6.22 MW).
                  The rate of steam generation, W  = Q          evap /[(h  − h ) + blowdown percent ×
                                                                              w
                                                         s
                                                                        s
               (h  − h )], where the symbols are as given earlier. Substituting, W  = 21.23 ×
                  t
                                                                                               s
                       w
                  6
               10 /[(1199.6 − 342) + 0.03 × (364 − 342)] = 24,736 lb/h (11,230 kg/h).
                  Determine the boiler economizer duty from Q              econ  = (1 + blowdown)(W )
                                                                                                           s
               (h   − h ),  where  symbols  are  as  before.  Substituting, Q        econ   =  1.03(24.736)
                  w
                         f
                                              6
               (342 − 196.3) = 3.71 × 10  Btu/h (1.09 MW).
                  The gas exit-temperature, T  = T  - Q        econ /TEG gas flow, lb/h)(l − heat loss)
                                                    3
                                                          2
               (heat  capacity,  Btu/lb  °F).  Since  all  values  are  known,  T   =  415  -  3.71  ×
                                                                                       3
                  6
               10 /(150,000  ×  0.98  ×  0.27)  =  317°F  (158°C).  Figure  11  shows  the
               temperature profile for this installation.

               Related Calculations. Use this procedure for heat-recovery boilers fired by
               gas-turbine exhaust in any industry or utility application. Such boilers may be

               unfired,  supplementary  fired,  or  exhaust  fired,  depending  on  steam
               requirements.
                  Typically, the gas-pressure drop across the boiler system ranges from 6 to
               12  in  (15.2  to  30.5  cm)  or  water.  There  is  an  important  tradeoff:  a  lower
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