Page 84 - Membranes for Industrial Wastewater Recovery and Re-Use
P. 84

64  Membranesfor lndustrial Wastewater Recovery and Re-use


              RSI = 2pHs - pH                                             (2.39)

          An RSI of  7 indicates a water more or less at equilibrium. As the value falls the
          water becomes more scaling and as it rises the water becomes more corrosive.
          The Langelier and Ryznar saturation indices can be used to predict scaling in
          most waters but they become unreliable when the total dissolved solids content
          approaches 5000  mg IF1.  Above  this  level  the Stiff  and Davis  index  (ASTM
          D4582) or a similar method must be adopted.
            Not  all  scale-forming  compounds  have  a  pH-dependent  deposition.  Some
          scalants have simple chemistry, analogous to that given in Equation (2.30):
              Mzf  + YZ-AMY                                               (2.41)


           or
               Mz+ + ZY-AMYz                                              (2.40)


           Scalants having the chemistry represented by Equation  (2.39) are mainly the
           sulphates of magnesium, barium and strontium (ASTM D4692).
             The simplest means of preventing scale formation in RO systems is to operate
           at a conversion sufficiently low that the reject stream is not so concentrated that
           solubility problems are encountered. This, of course, has economic implications
           for the operation of the plant that may be unacceptable, and in such cases some
           form of  scale prevention must be used. Where calcium carbonate or some other
           hydrolysable scalant is the main problem, i.e. those salts containing hydroxide
           (OH-)  and carbonate  (C032-)  which therefore  have  associated  pH-dependent
           solubility due to hydrolysis reactions (i.e. reaction with acid, H+) of these anions,
           it is often possible to adjust the LSI by acid dosing. This converts bicarbonate into
           carbon dioxide which can be removed  by  degassing  of  either the feed or the
           permeate. Depending on whether hydrochloric or sulphuric acid is used there
           will  be  an  increase  in  sulphate  or  chloride  concentration.  Increasing  the
           sulphate may give rise to calcium sulphate precipitation.
             Scale-inhibiting chemicals can be used to delay precipitation of some salts by
           interfering with the crystallization process forming microcrystals which do not
           cause fouling and which will not show significant agglomeration at least until
           the concentrate stream has left the RO unit. Most of the commercially available
           chemicals  work  well  on  calcium  carbonate,  provided  that  the  LSI  in  the
           concentrate  stream  is  less  than  +2, but  less  well  on  other  salts.  The  most
           established  scale  inhibitors  are  termed  “glassy  polyphosphates”,  typically
           sodium  hexametaphosphate  (Calgon@). These  work  by  absorbing  into  the
           nanoscopic protonuclei forming during the incipient stages of precipitation  and
           destabilising  the  subsequent crystal  nuclei.  They  are  not  the most  effective
           chemicals  for  the  application  and  revert  quite  quickly  in  solution  to
           orthophosphate, producing calcium phosphate sludge which can cause blocking
           of  separators and  small  bore  pipes.  Since  the development  of  Calgon,  more
   79   80   81   82   83   84   85   86   87   88   89