Page 256 - Design of Simple and Robust Process Plants
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242  Chapter 6 Process Design Based on Reliability
                The cost of theses outages may be high. Site vulnerability is discussed in the next chap-
                ter. Here, the results of a study by Shor and Griffin (1991) are summarized, regarding
                the design of co-generation plants to provide a reliable, continuous steam supply.
                  The objective for the study was to evaluate the reliability of steam supply of mini-
                mum 380 Mton/h for different co-generation design cases. Four design cases were
                considered, while case 2had a variant A and B (see Figures 6.9 and 6.10):

                  .   Case 1 consisted of three gas turbines (GT), frame 6, each provided with a
                      waste heat boiler (WHB) and two existing fossil boilers (FB).
                  .   Case 2 consisted of four gas turbines LM 2500 with WHB and two existing
                      fossil boilers.
                  .   Case 2 (A and B) differentiate themselves in the capacity of the WHB, 75
                      versus 100 Mton/h.
                  .   Case 3 consisted of three boilers with steam turbines provided with back-up
                      de-superheaters and the two existing FBs.
                  .   Case 4 emphasized four large-capacity boilers with three steam turbines pro-
                      vided with de-superheaters.
                The maximum steam and power capacities for these cases are summarized in
                Table 6.5. The steam production of these cases is also given if a boiler or a turbine is
                eventually combined with a WHB is out of service. In all these cases the minimum
                amount of steam (380 Mton/h) is still available. This is a design requirement, as
                utility plants have to provide their service all-year round, and so scheduled mainte-
                nance needs to be performed during operation. At a small site, the maintenance of
                utility systems might be performed during planned process plant stops. For the dif-



                   Case 1             Case 2A             Case 2B
                         100 t/hr              100 t/hr            100 t/hr
                 Boil 1               Boil 1               Boil 1
                         100 t/hr             100 t/hr             100 t/hr
                 Boil 2               Boil 2               Boil 2


                                              75 t/hr              100 t/hr
                        160 t/hr       LM                   LM
                                       2500  WHB            2500  WHB
                 Fr 6   WHB
                                              75 t/hr              100 t/hr
                                       LM                   LM
                        160 t/hr             WHB                  WHB
                                       2500                 2500
                 Fr 6   WHB                   75 t/hr              100 t/hr
                                       LM                   LM
                                       2500  WHB            2500  WHB
                        160 t/hr
                 Fr 6   WHB                    75 t/hr             100 t/hr
                                       LM                   LM
                                       2500  WHB            2500  WHB

                Fig. 6.9. Alternative designs for a co-generation plant.
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