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System design aids  183
















           rres5ure(r\1~)   1HH.5   136.1   156.1
           Osnotic  Pt'rl;sure(PSIG)   11.5   70.1   9.9
           NDP(Mean)-   146.8  PSlG
           Ruerage  Permeate  Flux=   14.6  GFD,  Permeate  Flou=  480.85  GPM   b
                      Recovery   Permate   Feed   Feed   Feed
           Rrray  E1.M.   (PernlFeed)  GPD MG/L   GPM   MGIL  PRESS(PSIG1
          71   1       .UP6   55A1   2   39.9   457  175.5
                       .lo3   5335   2   36.1   500  170.7
                       .111   5198   7   32.4   551  166.6
                       .177   5067   7   28.8   676   163.2
                       .I36   4945   3   25.3   713  160.5
               6       .153   4H33   3   71.9   874  158.3
            2  1       .W2   4547   3   34.4   973  151.7
               7       .a98   4394   4   31.2   1071  147.9              I_ j/
               3       .lo5   4252   4   28.2   1187  144.7
               4       .113   4117   5   25.2   1325  142.1
                       Figure 4.7  Sraling indices (Argo Analyzer, Betz-Dearborn)


        4.1.5 Overview
        Whilst RO CAD packages have become increasingly sophisticated and also more
        user friendly, more versatile and more widely  available over the years (Table
        4.3), it should be stressed that they cannot provide an alternative to pilot trails.
        Indeed, all suppliers emphasise that their software is intended to expedite design,
        rather than provide absolute values for the key process performance parameters
        with respect to the system hydraulics and permeate product water quality. None
        of the existing design packages are able to predict organic fouling or equate this,
        even by approximation, to some measurable feedwater quality determinant such
        as TOC. It is such determinants that have an impact upon crucial parameters as
        the pretreatment requirement, frequency and nature of membrane cleaning and
        membrane life. On the other hand, these CAD packages provide the option of
        designing  a  complete  RO  plant  under  what  could  be  considered  optimum
        conditions of  zero permanent fouling. In practice a more conservative process
        design and/or operation may well be called for.
          One obvious constraint on the use of  commercial software packages is their
        limitation  both  to  reverse  osmosis  and the  suppliers'  own products.  Several
        generic  RO,  and  more  recently  NF,  design  software  packages  have  been
        developed  over  the  years  by  academic  and  independent  research  groups
        worldwide.  An  example  of  a  pragmatic  MS  Visual  Basicm-based  software
        approach to handle the design and cost calculations for single pass cross-flow,
        feed and bleed  and semi dead-end  filtration systems, applicable to all types of
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