Page 224 - Membranes for Industrial Wastewater Recovery and Re-Use
P. 224

System design aids  193


            immediately  observes that the slope of  the limiting composite curve can only
            increase to the point at which the line touches the composite curve at the point
            (125, 50).  As such, the effluent concentration can only be allowed to increase up
            to  160 ppm, resulting  in an overall target  of  2.5 t/h. The limiting composite
            curve for the new problem is presented along with the water supply line and the
            pinch  point  in  Fig.  4.14.  It  is  observed  that  further  increasing  the  effluent
            concentration of Process 3 provides no further advantage.
              Whereas  Water provides a  graphical  presentation  of  the composite curves,
            thus allowing the engineer  to  tackle  the problem  graphically, WaterTarget
            provides a visual representation. Performing a so-called inlet sensitivity analysis,
            WaterTargetS pinpoints those processes and contaminants that may be adjusted
            so as to achieve an improved target. The result of this sensitivity analysis, which
            essentially  corresponds  to  the  graphical  analysis  described  previously,  is
            presented as a bar chart of cost saving in $/h per unit ppm concentration change
            for  each contaminant (Fig. 4.15). For  the example  given in this  section, the
            software  advises  the  engineer  that  it  is  beneficial  to  increase  the  inlet
            concentration of Contaminant 1 in Process 3. For this simple case, the bar chart
            is perhaps not necessary. For a more complex case, however, it provides a more
            accessible illustration of the system data. Indeed, whilst the theory is only valid
            for a single-contaminant  problem, the sensitivity analysis applies to multiple-
            contaminant cases.
              As already observed, the different approaches of fixed and non-fixed flow rates
            provide different solutions. To permit an increased effluent concentration from
            Process  3  and maintain  a  constant flow rate through  the process,  the  inlet
            concentration must be allowed to increase for the fixed flow rate approach. If

























                     0     50     IO0    150    200    250    300   350    400
                                             Mass load [t/h]
            Figure 4.14  Construction of water supply line for Contaminant  1 after relaxing the effluent concentration
            for Process 3
   219   220   221   222   223   224   225   226   227   228   229