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CHAPTER 11





                                      Industrial Applications



                                               and Case Studies






                          his chapter provides an overview of selected implementations
                          of the Process Integration methodology for various industrial
                     Tcase studies. The presentation is somewhat condensed because
                     of space limitations; more information is available in the works
                     cited.


                11.1  Energy Recovery from an FCC Unit
                     In this case study, the Heat Exchanger Network (HEN) of a Fluid
                     Catalytic Cracking (FCC) unit process consisted of a main column
                     and a gas concentration section (Al Riyami, Klemeš, and Perry, 2001).
                     The stream data was made up of 23 hot streams and 11 cold streams.
                     The associated cost and economic data required for the analysis were
                     specified by the refinery owners. Incremental area efficiency was
                     used for the targeting stage of the retrofit design. This was carried
                     out using the Network Pinch method (Asante, 1996; Asante and Zhu,
                     1997), which consists of a diagnosis stage and an optimization stage.
                     In the diagnosis stage, a few promising retrofit steps were generated
                     using the UMIST (now the University of Manchester) software
                     package SPRINT (2009). This software was also used to optimize the
                     initial design by trading off capital cost against energy savings. The
                     design options were then compared and evaluated, followed by
                     the final retrofit design proposed for final inspection.
                        The existing ΔT   of the process was identified as 24°C, and the
                                     min
                     hot utility consumption of the process was 46.055 MW; the area
                     efficiency of the existing design was 0.805. The potential for energy
                     saving was then derived from the resultant Composite Curves, which
                     are shown in Figure 11.1. As seen in the figure, the Composite Curves
                     are relatively wide apart except in the area around the Pinch.
                        The capital cost was estimated under the assumption that the
                     retrofit distribution of area would be the same as that for the
                     existing network. The resulting optimum minimum temperature
                     approach was found to be about 11.5°C for incremental α and about
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