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Page Title: MAINTENANCE
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OPERATION
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Stuffing  Box  Packing

Figure 9-4.—Nonpositive-displacement pump. centrifugal  pump  is  usually  located  below  the liquid  being  pumped.  (NOTE:  This   discussion assumes  a  constant  impeller  speed.) Figure  9-4  shows  that  when  the  pump  dis- charge  is  blocked,  nothing  happens  because  the impeller   is   hollow.   A   tremendous   buildup   in pressure  cannot  occur  because  the  passages  in  the impeller (between the discharge and suction side of the pump) act like a built-in relief valve. When the  discharge  pressure  and  pressure  head  are  equal (as in this case), the impeller is allowed to rotate (slips)  through  the  liquid  in  the  casing. NOTE:  Centrifugal  pumps  used  for  inter- mittent service may have to run for long periods of   time   against   a   blocked   discharge.   Friction between  the  impeller  and  the  liquid  raises  the temperature of the liquid in the casing and causes the  pump  to  overheat.  To  prevent  this,  a  small line is connected between the discharge and the suction  piping  of  the  pump. When a centrifugal pump is started, the vent line must be opened to release entrained air. The open passage through the impeller of a centrifugal pump also causes another problem. It’s possible for   liquid   to   flow   backwards   (reverse   flow) through   the   pump.   A   reverse   flow,   from   the discharge back to the suction, can happen when the   pressure   head   overcomes   the   discharge pressure  of  the  pump.  A  reverse  flow  can  also occur when the pump isn’t running and another pump  is  delivering  liquid  to  the  same  piping system.  To  prevent  a  reverse  flow  of  liquid through  a  centrifugal  pump,  a  check  valve  is usually installed in the discharge line. NOTE: Instead of two separate valves, some installations  use  a  globe  stop-check  valve. With  a  check  valve  in  the  discharge  line, whenever  the  pressure  above  the  disk  rises  above the pressure below it, the check valve shuts. This prevents liquid from flowing backwards through the  pump. MAINTENANCE.—   You  must  observe  the operation  and  safety  precautions  pertaining  to pumps  by  following  the  EOP  subsystem  of  the EOSS—if  your  ship  has  EOSS.  If  not,  use  the Naval  Ships’  Technical  Manual  (NSTM)  and/or the  instructions  posted  on  or  near  each  individual pump.   You   must   follow   the   manufacturer’s technical manual or MRCs for PMS-related work for  all  maintenance  work.  The  MRCs  list  in  detail what you have to do for each individual mainte- nance  requirement. Mechanical  Seals.—  Mechanical  seals  are rapidly  replacing  conventional  packing  as  the means   of   controlling   leakage   on   centrifugal pumps.  Pumps  fitted  with  mechanical  seals eliminate  the  problem  of  excessive  stuffing  box leakage,  which  can  result  in  pump  and  motor bearing  failures  and  motor  winding  failures. Where  mechanical  shaft  seals  are  used,  the design  ensures  that  positive  liquid  pressure  is supplied to the seal faces under all conditions of operation and that there is adequate circulation of  the  liquid  at  the  seal  faces  to  minimize  the deposit  of  foreign  matter  on  the  seal  parts. One type of mechanical seal is shown in figure 9-5. Spring pressure keeps the rotating seal face Figure 9-5.—Type-1 mechanical seal. 9-4

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