Page 227 - Know and Understand Centrifugal Pumps
P. 227

Know and Understand Centrifugal Pumps


          The pump  shaft  must  be  free  to slide through  the  O-ring. However,
          crystallizing liquids,  accumulated solids and pastes,  and products  that
          harden can cause the O-ring to hang-up or stick to the shaft losing its
          freedom. Oversized shafts and sleeves can also be blamed. If the seal is
          misaligned onto the shaft the O-ring can fret the shaft and hang into its
          groove. Heat and chemical attack can also make the O-ring vulcanize to
          the  shaft.  Any  of  these  can  occur.  As  the  shaft  moves  within  the
          tolerance of the bearings, it can drag the seal faces open or crush them
          together if the O-ring sticks to the shaft.


        The springs clog and jam


          Suspended solids, crystals and sediment in the pumped liquid can lodge
          into  the  seal  springs  and  restrict  their  movement.  Jammed  springs
          cannot  flex  to  maintain  the  seal  faces  united  while  the  shaft  moves
         within  the  bearing  axial  tolerance.  It’s  best  to  use  seals designed  for
          slurries  and  solid  particles.  Many  of  these  designs  have  the  springs
          placed outside the pumped  fluid. The seal chamber design and piping
          also has an influence on the seal’s ability to survive while handling solid
          particles. Seal chambers designed with tapered, spiraled, and open bores
          facilitate the handling of suspended solids (Figure 14-9).
         The discharge re-circulation line is a dinosaur of design, held over from
          the days when pumps had packing. With packing, the discharge bypass
          line prevented the entrance of air through the packings on pump start-
          up,  and  also  provided  some  cooling  to  the  packing  rings.  With  a
          mechanical  seal  in  slurry service, this  discharge  bypass line  blasts  the
          mechanical seal and chamber with the highest concentration of solids in
          the pump.  It will destroy the seal in short order. If some cooling and
          flushing is desired, a suction bypass line, from the seal chamber to the
         pump suction nozzle, is preferred over a discharge bypass line, from the
          pump discharge to the seal chamber.







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        Fiaure 14-9


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