Page 24 - Membranes for Industrial Wastewater Recovery and Re-Use
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lntroduction  5


           Table 1.2  Generalised industrial water quality standards
           Class:       3     4        5        6        7       8       9
           Type:        Softened  Dealkalised  Deionised   Purified   Apyrogenic  High   Ultrapure
                                                                 purity
           Conductivity,                 20       5       5        0.1     0.06
           N/cm
           Resistivity,                  0.05     0.2     0.2     10      18
           MS2  cm
           TDS. mg/l                   < 10      Cl      <l        0.5     0.005
           PH                             5.0-9.5   6.0-8.5   6.0-8.5   6.5-7.5
           LSI          -1to+l  -1to+l
           Hardness,    < 20             0.1     <0.1    <0.1              0.001
           mg/l CaC03
           Alkalinity,         < 30                                        0.001
           mg/l CaC03
           Ions, mg/l                                                      0.001
           Silica, mg/l                  0.5      0.1     0.1     < 0.01   0.002
           TSS, mg/l                    <0.1     <0.1    <0.1     <0.1    ND
           Turbidity, NTU               < 0.5
           SDI                          <5       <3      13       <l      < 0.5
           Particle count,                        1       1        1       0.1
           no./ml
           COD, mg/l                             <O.l    <0.1
           TOC, mg/l                                                       0.05
           Microorganisms.                      < 10     <1       <I      <1
           cfu/ml
           Pyrogens, EU/ml                               <O.25            < 0.25


           15 years  from  €1.48  [$2.12] in  1984-85  to  €4.90  [$7.94] in  1999-2000
           (Water UK, 2000). In more arid regions of the world the figure is higher: between
           1980 and 1995 water costs increased  by  more than an order of  magnitude in
           California  (Mannapperema  et al., 1993). It is  clearly  of  some cost  benefit  to
           acquire a source of water that is commensurate with the quality demanded for its
           end usc, without increasing freshwater demand or discharging waste to sewer.
           The economic viability  of  existing municipal effluent reclamation  is then very
           much  dependent  on the match  between  the effluent  water  quality  and that
           demanded by the duty.
             A whole industry has built up around the above key concept. Pinch analysis
           has conventionally been employed to maximise heat transfer efficiency within an
           industrial process. Water pinch analysis (Baetens, 2002; Section 4.2) is simply
           pinch  analysis based on water quality and volumes, i.e. based solely on mass
           rather than heat. As such, it is simply an extension of  a simple water audit. On
           the other hand, water pinch  analytical  tools have not yet  reached  a level of
           sophistication  where  water  purification  unit  processes  can  be  incorporated,
           since the performance of such processes can rarely be reliably predicted.
             Volumes of water used are actually extremely dependent upon the policy of the
           company  or  the  individual  factory  regarding  water  management,  and  in
           particular their housekeeping. Housekeeping relates to the way individual unit
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