Page 288 - Membranes for Industrial Wastewater Recovery and Re-Use
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Case studies  2 5 7

           permeate (Table 5.20). Suspended solids and n-hexane extractable compounds
           are  similarly  reduced  from  1120  and  475  mg 1-1  to  less  than  1 mg 1-1
           respectively. The final RO stage produces a permeate with a final conductivity of
           125 pS  cm-l.
             Combined water and sewerage charges in the city of Yokosuka are 4607 mP3
           ($4.1 5 m-3). The plant operates for 260 days per years and so the installation
           and  operation  of  the  reuse  plant  results  in  a  direct  saving  (Table  5.11) of
           420 338 000 ($139 315) per annum with an additional Y1400000 ($9590)
           saved through reduced chemical demands on the boiler system. The total annual
           costs of  running the additional treatment technology  is Y5 406 300 ($37 033)
           resulting in a net  annual saving of  Y14 931 700 ($102 282). The cost of  the
           plant is covered by offsetting 43 000 000 ($20 550) per year as depreciation  on
           the plant over its projected lifetime yielding a true annual saving of Yl1 93 1 700
           ($81 732).




           5.9 Pasfrost vegetable processing plant (Belgium)


           5.9.7 Background
           Pasfrost. located  in Passchendaele, western Belgium, is a vegetable processing
           company producing 65 000 tonnes of deep-frozen vegetables per year. The plant
           processes  a wide  variety of  vegetables  depending on the season  ranging from
           squashes and leaf crops in the summer to root vegetables in the winter. Process
           water  is  used  at  the  site  for  a  range  of  activities  such  as  washing/rinsing.
           blanching, steam peeling, caustic peeling and cooling.
             Traditionally,  water  is  supplied  from  groundwater  sources  that  are
           bacteriologically safc and rcquire no treatment prior to use. However, economic
           development in the region has led to increasing pressures on the ground water
           sources resulting in the need to abstract from wells over 300 m deep. The quality

           Table 5.11  Cost sheet for wastewater treatment reuse plant (as of 1998)

                                          Annual cost (Y)       Annual saving (Y)
           MBR energy (120 m3 d-l)          925 500 (6339)
           MBR membrane (120 m' d-')      3 600000 (24 660)
           RO energy (40 m3 d-')            280800(1923)
           RO membrane (40 m3 d-' 1         600000 (4110)
           Totalopex(Ymm-3)                  205.8 (1.4)
           Reduced water charges                                 9 469 200 (64 864)
           Reduced sewage charges                                9 469 200 (64 864)
           Reduction in boiler chemical costs                    1 400 000 (9590)
           Total                           5406 300 (37033)     20 338 000 (139 31 5)
           Currency conversion  ( x  0.00685) based  on 12 August 1998 figures (http://www.oanda.com/convert/
           fxhistory (accessed November 2002)).
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