Page 285 - Membranes for Industrial Wastewater Recovery and Re-Use
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254  Membrnnesfor  Induslrial Wastewater Recovery and Re-use

           0.001 across all the consented wavelengths. Heavy metal removal was also very
           good with chromium concentration reducing from 0.75 to less than 0.02 mg 1-l.
             The installation of  the plant was required by changes to discharge consents
           but the ability to recycle water within the plant provided a number of  economic
           advantages to ensure the scheme became financially viable. Major savings were
           achieved in the cost of  softened mains water  (by 95%) and the reduction of
           effluent charges.  A  less obvious saving  was  made  by  the  reduction  in  heat
           demand achieved by recycling the previously heated water within the process.
           The capital cost of  the schemes was €275  000 ('5448 800) in  1998 and the
           annual net saving on the reuse plant was €142 635 (5232 780) resulting in a
           payback  time of  1.9 years  (Table 5.10). The company  ceased  production  in
           March 2001 at which point the quarterly effluent bill had reduced from €12 481
           ($1 7 723), prior to the reuse plant, down to €640 ($908). Overall the decision to
           install the plant resulted in a profit to the company of €182 067 ($258 535) over
           its operational life.



           5.8 N food plant wastewater treatment and recycling plant (Japan)


           5.8.7 Background
           Yokosuka city, situated in the Kanagawa Prefecture has no nearby rivers and
           as such water is supplied from water treatment plants situated on the Sagami
           river a distance of  30 km away. N company is a producer of  frozen foods (such
           as Chinese and Japanese dishes) and is situated within Yokosuka city and so


           Table 5.10  Cost sheet for dye bath reuse scheme (as of 1999)
                                         Annual cost, f. (S)      Annual saving, € ($)
           Membrane replacement           29 714 (47 806)
           Prefilter opex                  1408 (2265)
           Labour                          5760 (9267)
           Power                          22 464 (36  142)
           Water                           2661 (4281)
           Cleaning chemical                960 (1 544)
           Maintenance                     3679 (5919)
           Chlorine dioxide treatment     37 058 (59 622)
           Total opex E mM3                 1.07(1.72)
           Effluent disposal                                       60015 (96 558)
           Water                                                   68 874(119 811)
           Water softening                                          9316 (14988)
           Colour charge                                           56 828 (91 430)
           Water heating                                           50 307 (80938)
           Total                         103 705 (166 850)        246 340 (396 336)
                 ~
           Currency conversion  (x 1.608) based  on 12 August  1999 figures (http://www.oanda.cOm/convert/
           fxhistory (accessed November 2002)).
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