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The  Practical  Pumping  Handbook   ~   :::::   -   -:  ::~c---~


       Many of these  more  aggressive liquids  can produce  toxic fluid exposure
       and  vapors  if  they  are  allowed  to  leak  out  of  a  pump.  For  example,
       vapor  release  is  a  common  danger  with  hydrocarbons  that  vaporize  at
       atmospheric  conditions  or other  chemicals that  may be  exposed to very
       high  operating  temperatures.  If  a  vapor  release  is  exposed  to  a  spark,
       the vapor cloud may even explode or catch fire.
        Consequently,  in handling these liquids, we must  be  extremely aware of
       much  more  than  environmental  damage  and  pumping  efficiency.  We
        must also be very conscious about personal safety. Therefore,  the choice
        between the ANSI  pump  and the API pump  must take into  account the
        specific  fluid  properties,  as well  as  the  operating  conditions.  The  main
        difference  between  these  pumps  is  predominantly  a  result  of  the
        differences in casing design.



      1.3  Pump  cases


        Both  pump  styles  have  a  radial  split  casing,  and  most  smaller  pump
        cases  employ  a  single  volute  design  of  the  interior  passages.  This  is
        particularly  evident with  low-flow rates  and  lower  specific speeds  of the
        impeller.
        As  shown  in  Figure  1.3,  the
        impeller  is offset within  the  volute
        design and  that point  in the  casing
        that  is  closest  to  the  impeller  is
        referred  to  as  the  'cut-water'.  In  a
        counterclockwise  direction  from
        this  point,  the  scroll  design  of the
        casing  wall  steadily  moves  away
        from  the  impeller  around  its
        perimeter.  This develops the pump
        capacity  throughout  the  rotation
        until  it  exits  the  discharge  nozzle
        located on  the pump  centerline.   Figure 1.3. Single Volute Casing

       As  the  wall  of  the  casing  retreats
       from  the  impeller,  the  area  of the
       volute  increases  at  a  rate  that  is  proportional  to  the  rate  of discharge
       from  the  impeller,  thus  producing  a  constant  velocity  at  the  periphery
        of  the  impeller.  This  velocity  energy  is  then  changed  into  pressure
       energy by the  time  the  fluid enters the  discharge  nozzle.
       The  peculiar  shape  of  the  volute  also  produccs  an  uneven  pressure
       distribution  around  the  impeller,  which  in  turn  results  in  an  imbalance
       of the  thrust  loads  around  the  impeller  and  at right  angles  to  the  shaft.



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