Page 227 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 227

Pumping of Liquids                                       197

                                                                fixed  condition  of suction  lift,  and  relates  speed,  head
                         '  I           ii                      and capacity.  This index is a valuable guide in establishing
                                        "'1"      I              the maximum suction lifts and minimum suction heads to
                                        1e    t-r               avoid  cavitation  of the  impeller  with  resultant  unstable
                                         I
                                                                 hydraulic  performance and  physical  damage.  For a  given
                                  --;;�icSl'f.f.0
                     � -       -                                set of conditions on the suction and discharge of a pump,
                 01,--               I                          a slow rotative speed will operate safer at a  higher suction
                                                                 lift than a  pump of higher rotative speed.


                IIO                     -                       Rotative Speed
                     HEAD-CAPACITY   ,,.   ,........,
                llO   '                      \\""
                                                                   The  rotative  speed  of a  pump  is  dependent upon  the
                            --p<  r--,.....
             ..,   l40     .>./                  \              impeller  characteristics,  type  fluid,  NPSH  available  and
             �
             ...
             ...
                               l'OIIIT  �
                                        i,.,,--  '�
             :!   L      "'  ,.�  #--  IIAill-  �  �   I   \    other factors  for its final  determination. The  most direct
                                ["1CI[..,
                                     ,,.,.....
             ;,::."   ·--   4J,              '  \                method  is  by  reference  to  manufacturer's  performance
             d
            ..,        J  ,,,,,   ...,  K"'   "'"  '\            curves.  When  a  seemingly  reasonable selection  has been
                                              I
            c
                                              I
             ..,
             :r:.   IO   L.-                  I  I   "  \   40   made, the effect of this selected speed on the factors such
            e   eo                I           I  I        L      as NPSH required,  suction head or lift,  fluid erosion and
            c
                40   J                        11  I     ZO.:-    corrosion, etc., must be evaluated.  For many systems these
                                                          z
                to  I                         I  I      10•     factors are of no concern or conseqt,ence.
                  I                           I                    Normal  electric  motor speeds  run  from  the  standard
                 0                            I          0       induction speeds for direct connection of 3600,  1800 and
                  0   !   4   I   (!   10   12   14   II  111   ZO  22
                                                                 1200  rpm  to  the  lower  speed  standards  of the  synchro-
                           CAPACITY,  !N  100 CiPM
                                                                 nous motors,  and then  lo  the  somewhat arbitrary  speeds
           Figure 3-50. Typical centrifugal  pump characteristic curve with aux-   established  by  V-belt or gear drives.  For some  cases,  the
           iliary  specific  speed  curve.  Double-suction,  single-stage,  6-in.   pump speed is set by  the type of drivers available,  such as
           pump,  operating  at  1760  rpm  constant  speed.  (By  permission,   a gasoline engine.
           Karassik,  I.  and  Carter,  R.,  Centrifugal Pumps,  McGraw-Hill  Book   Electric  motors  in  pump  application  never run  at the
           Co.,  inc.,  1960,  p.  197.)
                                                                 "standard" rotative design speeds noted above,  but rotate
                                                                 at about (with some deviation)  3450,  1750, and  1150 rpm,
           ciency.  Figure  3-4 7  illustrates  the  range  of typical  specific   which are  the speeds  that most pump manufacturers  use
           speed index numbers for particular types of impellers.   for their performance curves.  If the higher numbers were
                                                                 used  (motor designated or name plate)  for pump perfor-
           Example 3-12:  "Type Specific Speed"                  mance  rating,  the  pumps  would  not meet  the  expected
                                                                 performance,  because  the  motors  would  not be  actually
             In Figure  3-50,  where  the pump operates  at 1760  rpm   rotating fast enough  to  provide the characteristic  perfor-
           (a standard  motor speed under load)  and has  maximum   mance curves for the specific size of impeller.
           efficiency at 1480 GPM and 132 feet head,  the  "type" spe-
           cific speed is                                                 Pumping Systems and Performance
                                                                   It is  important to recognize  that a  centrifugal pump  will
                                                       (3- 11)   operate  only  along  its  performance  curve  [10,  11).  External
                                                                 conditions  will  adjust themselves,  or must be  adjusted  in
                                                                 order to obtain stable operation. Each pump operates  within
                   [1760'\ � ]                                   a  system,  and  the  conditions  can  be  anticipated  if each
             N                    1740
               s
                     (132)0,o                                    component part  is  properly  examined.  The  system  con-
                                                                 sists of the friction losses of the suction and the discharge
                                                                 piping plus  the total  static  head from suction  to final dis-
             Figure  3-47  indicates  the  general  type  of  impeller   charge point.  Figure 3--51  represents a  typical system head
           installed.
                                                                 curve  superimposed  on  the characteristic  curve  for a  10
             The  specific  speed  of  a  given  type  pump  must  not   by 8-inch pump with a  12-inch diameter impeller.
           exceed  the  specific  speed  values  presented  by  the   Depending upon the corrosive or scaling nature of the
           Hydraulic  Institute  [17].  This  is  based  on  a  known  or   liquid  in  the pipe,  it may  be  necessary to  take  this condi-
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