Page 201 - Membranes for Industrial Wastewater Recovery and Re-Use
P. 201

170  Membranes for Industrial  Wastewater Recovery and Re-use


          Table 3.39  Highly puriRed water (non-cornpendial water)
          Parameter               Units               USP 25         Ph. Eur. (bulk)
          TOC                     ppb C                               500
          Conductivity            pS/cm at                            < 1.1
                                  20°C
          Aerobic bacteria        CFU/ml                             < 10
          Bacterial               EU/ml                               <0.25
          endotoxins


          and  costs  of  water  and  effluent  disposal  increase, the  latter  being  almost
          inevitable.
            It is nonetheless technically possible to reuse effluent at present to generate a
          usable feed stream, especially given that around 45% of the wastewater is likely
          to have an aggregate conductivity of well below 100 pS cm-l, based on the data
          given in Table  3.39, and would  thus actually dilute the mains water supply.
          Much of the effluent produced from pharmaceutical processes has a limited range
          of contaminants, namely only trace levels of the products being manufactured
          and very  low  levels  of  salts and organics.  Also,  this effluent  is  much better
          characterised and controlled than typical municipal-supplied  drinking water,
          since PW and WFI waters are very low in dissolved matter and the exact nature
          of  the  impurities  added  are  known.  Consequently,  it  should  be  possible  to
          specifically monitor and, if  necessary, selectively remove individual impurities
          introduced from the production environment into the effluent to ensure that the
          reclaimed water consistently meets the drinking water standard.
            For example, PW typically has a conductivity < 1 pS  cm-l, i.e. a total dissolved
           solids concentration of  around 0.5 mg 1-l.  This content is largely made up of
           sodium  and chloride  ions with traces of  potassium,  fluoride  and other small
           molecular weight ions. If  this water is used in the final rinse of a process vessel
          the only contaminants added will be residual quantities of  the products being
          manufactured, generally  at levels  < 1 mg 1-l.  The  actual quantities of  these
           products will be accurately measured and recorded as part of the validation of
           the CIP process but will obviously vary  between  applications. The impurities
           from other waste streams will generally be the same as those present in the feed
          water but at much lower levels, and can be measured using the same analytical
           methods as are used for potable water.
             Water  continues  to  be  the  most  commonly  used  chemical  in  most
           pharmaceutical operations and also continues to be one of the most problematic.
           One of the largest causes for product recalls are water-related issues, and such an
           environment imposes a considerable barrier to water recycling. If there is also no
           strong economic  driving force, regardless  of  the technical feasibility  of  water
           recycling, it is unlikely to happen in this industry in the near future.
   196   197   198   199   200   201   202   203   204   205   206