Page 350 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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318                       Applied Process Design for Chemical and Petrochemical  Plants


           C.  n  =  0.667;  equal  mass transfer rate        input horsepower of motor and  speed  of agitator.  Select
             More  directly  related  to  turbulence  and  motion  at   the calculated point in the grid,  then move to the nearest
             the interface.  Includes scale-up for rate of dissolving   speed  and  input  horsepower  (not  motor  hp).  Usually
             of  solids  or  mass  transfer  between  liquid  phases.   adjustments from actual design will be required, but often
             Using geometric similarity and equal power per vol-   the  incremental  adjustments will  not be  great.  To  aid in
             ume results in same n value.                     these  adjustments,  equal  torque  will  give  equal  liquid
           D. n  =  0.5;  equal surface motion                motion or solids suspension over a  narrow  range.  To use
             Related to vortexes formation, depth of vortex relat-   equal  torque,  set  up  diagonals  from  lower  left  to  upper
             ed to geometric similarity and equal Froude number.   right for the available equipment. Adjust or back-calculate
           E. N  =  O;  equal blend time                      (if necessary)  the expected performance and dimensions
             Rarely  used  due  to  large  equipment  required  to   based  on  the  adjustment.  Higher  speeds  require  higher
             hold speed constant for larger units.            horsepower.  For  equivalent  mass  transfer,  equal  power
                                                              changes are used.
           For turbulent power,  (constant power number,  P 0):   To  recheck  final  design,  the  diameter  of  a  single,
                                                              pitched blade turbine, for turbulent conditions:
           p P  Ns os                                 (5-49)

          Vp  0 3                                     (5-50)                                               (5-54)

           P/V p  N 3 D 2   (power per volume)        (5-51)   OT= impeller diameter,  turbulent operation, in.

           For P /V constant in two different systems,  then   Php  =  horsepower used by system  (not motor horsepower
                                                                   of driver)
                                                      (5-52)   Sg  =  specific gravity of fluid
                                                               N  =  agitator impeller speed,  rpm
                                                      (5-53)

        Figure  5-33  provides  a selection  grid  for establishing  the   Of course economics enters  into the solution, so some
        industrial  standard  for  the  driving  equipment,  that  is,   alternate designs may be helpful.




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                                                        C.lcullted horlepowers,  hp
        Figure  5-33.  Scaled-up  horsepower/speed  requirement for  an  agitator  system  is  readily  related  to  industrial  equipment.  By  permission,
        Rautzen,  R.  R., et al.,  Chem.  Engr.,  Oct.  25,  1976,  p.  119 (32].
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