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                     5.6.2  Illustrative Example: A Brewery Plant
                     This section discusses the case study of a brewery plant (Tokos and
                     Novak Pintarič, 2009) as a means to illustrate how mathematical
                     optimization is used to solve water minimization problems. In the
                     brewery studied, the ratio (by volume) of process water consumed to
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                     product beer sold was 6.04 : 1; this translated into 653,300 m /y of
                     water consumed. In terms of the ratio set by BREF (2006), this
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                     freshwater consumption exceeded the upper limit by 144,900 m . In
                     light of these figures, the company undertook to improve its process
                     by retrofitting modifications to its existing water network so that the
                     plant’s usage of freshwater would be minimized.
                        Production at the brewery plant involves a mixture of water-
                     using batch and semicontinuous processes. Water-using operations
                     in the packaging area are operated mainly in batch mode, with the
                     exception of rinsers for nonreturnable glass bottles and cans.
                     Wastewater stream from semicontinuous processes can be reused in
                     batch processes with a lower purity requirement. Hence, the basic
                     formulation first proposed is designed to enable the efficient
                     integration of semicontinuous and batch water-using processes.
                        The continuous wastewater streams are treated as limited
                     freshwater sources, and the unused wastewater is discharged. In the
                     next step, the model is extended by including options for installing
                     intermediate storage tanks for the collection of unused wastewater
                     streams for reuse over subsequent time intervals. This particular
                     design modification is motivated by differences in the operating
                     schedules of the filling lines. The superstructure representation for
                     water reuse and regeneration reuse (as defined in Section 5.2.4) is
                     depicted in Figure 5.5.
                        Opportunities for regeneration reuse were analyzed in the
                     brewhouse and in the cellar (see Figure 5.6), since these processes
                     were characterized by a high concentration of contaminants. Here
                     the basic model is extended by installing a local (on-site) wastewater
                     treatment unit that can operate in either batch or continuous mode,
                     thereby enabling water regeneration reuse and recycling. The
                     scheduling of batch wastewater treatment units is performed
                     simultaneously so that the treatment schedule will coincide with the
                     fixed schedule of the batch process. The design includes the option to
                     install storage tanks before and after treatment; this enables
                     wastewater and/or purified water to be stored until required by the
                     treatment schedule.
                        As reported in Tokos and Novak Pintarič (2009), the integration
                     of the water network in the packaging area made it possible for
                     wastewater from the can rinser to be reused in the pasteurization
                     processes. In this way, freshwater consumption could be reduced by
                     23 percent and the common costs of freshwater and wastewater
                     treatment by 22 percent. These improvements do not require the
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