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Pro c ess  O p timization  35


                     Network and Topology Data Identification
                     Obtaining network-related information is needed to account for
                     constraints that are related to the system topology and to the limits
                     imposed by operating units on the suitability of various process
                     streams to serve as inputs or outputs. In water networks, such
                     considerations include the acceptability (or unacceptability) of using
                     the water output from some operations as inputs for other operations.
                     For instance, the final washing of sugar crystals in sugar production
                     would require pure water, and for this the outputs from other water-
                     using operations would be unacceptable. On the otherhand, used
                     water from blanching might be perfectly acceptable for the initial
                     washing  or  rinsing of fruits. This type of information is used to
                     formulate  additional  constraints on the compatibility of different
                     process streams. When supplied to automated process optimization
                     algorithms, these constraints serve to eliminate a number of infeasible
                     combinations of process units. When building pure MPR models
                     (Williams, 1999), network-related information is transformed into
                     explicit mathematical constraints involving expressions with binary
                     selection variables. When using the graph-theoretic approach and/or
                     the P-graph framework (Friedler et al., 1993) to construct a process
                     model, such information is explicitly encoded in the P-graph building
                     blocks (materials and operations) and is then used by algorithms that
                     generate only those topologies that are combinatorially feasible.

                     3.10.2   Mathematical Modeling of Processes:
                              Constructing the Equations
                     After the conceptual basis has been established, it is time to begin
                     constructing the explicit mathematical formulations of the problem.
                     The standard procedure in this regard is first to build a super-
                     structure—one that incorporates all possible options and combin-
                     ations of operating units—and then to reduce the superstructure via
                     optimization techniques. In this context, a superstructure is the union
                     of several feasible flowsheets (see Figure 6.2 for an example of a water
                     reuse network superstructure). When this union includes all possible
                     flowsheets, the superstructure is called the  maximal structure
                     (Friedler et al., 1993) or the  hyperstructure (Papalexandri and
                     Pistikopoulos, 1996).
                        There are two basic approaches to formulating the superstructure
                     and subjecting it to reduction optimization.
                         1.  Explicit formulation of a superstructure by the design engineer,
                            followed by translation of that structure into an integer programming
                            model: The generated problem is then solved by the
                            corresponding MPR algorithm. Popular codes for solving
                            MILP problems are OSL (GAMS, 2009) and CPLEX (ILOG,
                            2009); both are included in such commercial optimization
                            software packages as GAMS (2009). If the model does not
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