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I n d u s t r i a l  A p p l i c a t i o n s  a n d Ca s e  S t u d i e s   267


                     regeneration unit that is not part of options A and B. These results
                     are summarized in Figure 11.9.
                        Design options A and D are the most attractive ones in terms of
                     maximizing both reuse and regeneration reuse. Option A results in a
                     smaller reduction in freshwater use but at a lower investment cost
                     than option D, which results in a larger reduction in freshwater use
                     but at a much higher investment cost. Wastewater reductions are
                     proportional to freshwater reductions, with corresponding reductions
                     in wastewater treatment costs for each of the options. The cost
                     analysis carried out for design option A indicates attractive financial
                     returns for this low-investment option, whose payback period is only
                     0.14 years. The outlet water quality of operation 3 required further
                     analysis, so a complete cost evaluation of design option D was not
                     possible. Fully evaluating this option would require additional
                     detailed studies to identify the regeneration process type required
                     and its associated costs.
                        The heat energy of the reuse water streams proposed in the
                     design options was reviewed to ensure that stream temperatures at
                     the inlet of operations remained unchanged. Citrus plant managers
                     reported that nearly all of the process operations occur at ambient
                     temperatures; the only exception was operation 8, which produces
                     wastewater at 90°C. (This particular waste stream is highly
                     contaminated, which imposes some limitations.) All the water reuse
                     streams proposed by the four design options are at appropriate
                     temperatures, so they should not have a thermal effect on operations.
                     The overall hot and cold utility requirements of the plant would not
                     be affected by the changes proposed in the design options.
                        With its existing water network, the plant consumes 240.3 t/h of
                     freshwater and generates 246.1 t/h of wastewater. The proposed
                     design options offer a 30 percent and a 22 percent reduction in
                     freshwater consumption and wastewater generation. For a practical
                     project, the number of modifications is limited. The maximum water




                                       FRESHWATER SAVINGS
                     Number of
                     New Pipes   Theoretical Freshwater Reduction Limit, 31%  % Feed Water
                      Required                                      Reduction
                                                                    30
                                                    30        30
                                                                    25
                                 22        22                       20
                                                     9
                           10              7                  7
                                  5
                            5
                                  A        B         C        D
                                           Design Options

                     FIGURE 11.9  Summary of four design options.
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