Page 188 - Sustainability in the Process Industry Integration and Optimization
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CHAPTER 8





                                                            Combined



                                         Process Integration



                                              and Optimization







                8.1  The Role of Optimization in Process Synthesis

                     Process Integration (PI), as defined in Chapter 2, is a family of
                     optimization methodologies for reducing resource or emissions
                     intensity of the analyzed processes and Total Sites. As such, it is
                     tightly related to optimization. In fact, PI and optimization
                     complement each other by their functionality. First, PI sets out the
                     strategy for designing and/or operating industrial processes. This
                     gives engineers some direction regarding how processes can be
                     designed or changed, answering the questions of “where we can go?”
                     and “what is to be done?” in order to achieve the business goals at
                     hand. In addition, PI provides quantitative targets for designers and
                     engineers; it does this by exploiting the physical (in the case of Heat
                     Integration, thermodynamical) background to answer the question
                     “how much is it possible to improve or achieve?” The targets in most
                     cases are upper bounds on the process performance or lower bounds
                     on the extent of resource use or emissions. In many cases the targets
                     are practically achievable, as in the case of designing Heat Exchanger
                     Networks (HENs) or water networks. The most obvious example is
                     heat recovery targets established by the Pinch point when analyzing
                     HEN problems. Since they are based on the Second Law of
                     Thermodynamics, it is proven that better heat recovery cannot be
                     achieved by any feasible system. If a realistic value for ΔT   is
                                                                          min
                     specified for their evaluation, the targets will be also practically
                     achievable. Of course, the additional factor of the capital costs for
                     implementing the heat exchangers generally tends to shift the
                     economic optimum of the designed HEN away from the maximum
                     recovery network.


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