Page 16 - Chemical Process Equipment - Selection and Design
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RULES  OF THUMB:  SUMMARY



             Although  experienced  engineers know  where  to  find  information   9. Compression ratio should be about the same in each stage of  a
             and how to make accurate computations, they also keep a minimum   multistage unit, ratio = (P,JPl)l'n, with n stages.
             body  of  information  in  mind  on  the  ready,  made  up  largely  of   10.  Efficiencies of  reciprocating compressors: 65% at compression
             shortcuts and rules of  thumb. The present compilation may fit into   ratio of  1.5, 75% at 2.0,  and 8045% at 3-6.
             such a minimum body of  information, as a boost to the memory or   11. Efficiencies  of  large  centrifugal  compressors,  6000-100,000
             extension in some instances into less often encountered areas. It is   ACFM at suction, are 76-78%.
             derived from the material in this book and is, in a sense, a digest of   U. Rotary compressors have efficiencies of 70%, except liquid liner
             the book.                                             type which have 50%.
                An  Engineering  Rule  of  Thumb  is  an  outright  statement
             regarding suitable sizes or performance of  equipment that obviates   CONVEYORS FOR  PARTICULATE SOLIDS
             all need for extended calculations. Because any brief statements are
             subject  to  varying  degrees  or'  qualification, they  are  most  safely   1.  Screw  conveyors  are  suited  to  transport  of  even  sticky  and
             applied by engineers who are substantially familiar with the topics.   abrasive  solids  up  inclines  of  20"  or  so.  They  are  limited  to
             Nevertheless, such rules should be of  value for approximate design   distances of  150ft  or  so  because  of  shaft  torque  strength.  A
             and  cost  estimation,  and  should  provide  even  the  inexperienced   12 in.  dia  conveyor  can  handle  1000-3000 cuft/hr,  at  speeds
             engineer  with  perspective  and  a  foundation  whereby  the  reason-   ranging from 40 to 60 rpm.
             ableness of  detailed  and  computer-aided  results can be  appraised   2.  Belt conveyors are for high capacity and long distances (a mile or
             quickly, partitcularly on short notice such as in conference.   more,  but  only  several hundred  feet in a plant), up inclines of
                Everyday activities also are governed to a large extent by  rules   30"  maximum.  A  24in.  wide  belt  can  carry  3000cuft/hr  at  a
             of  thumb.  They serve us when we  wish  to take  a course of  action   speed  of  100 ft/min,  but  speeds up  to 600 ft/min  are  suited to
             but are not in a position to find the best course of  action. Of interest   some materials. Power consumption is relatively low.
             along this line is an ainusing and often useful list of  some 900 such   3.  Bucket elevators  are  suited  to  vertical transport  of  sticky  and
             digests of  everyday experience that  has been  compiled by  Parker   abrasive materials. With buckets 20 X 20 in.  capacity can reach
             (Rules of  Thumb  Houghton Mifflin, Boston, 1983).    lOOOcuft/hr at  a  speed of  100ft/min, but  speeds to 300ft/min
                Much  more can be  stated in adequate summary fashion about   are used.
             some  topics  than  about  others,  which  accounts  in  part  for  the   4.  Drug-type conveyors (Redler) are suited to short distances in any
             spottiness of  the present coverage, but the spottiness also is  due to   direction and are completely enclosed. Units range in size from
             ignorance and  oversights on  the  part  of  the  author.  Accordingly,   3 in. square to  19 in.  square and may travel from 30 ft/min  (fly
             every engineer undoubtedly will supplement or modify this material   ash) to 250 ft/min (grains). Power requirements are high.
             in his own way.                                    5.  Pneumatic conveyors are for high capacity, short distance (400 ft)
                                                                   transport  simultaneously  from  several  sources  to  several
                                                                   destinations.  Either  vacuum  or  low  pressure  (6-12 psig)  is
             COMPRESSORS AND  VACUUM  PUMPS                        employed with  a  range  of  air  velocities from  35  to  120ft/sec
                                                                   depending on the material and pressure, air requirements from 1
             1. Funs  are used  to raise  the  pressure  about  3%  (12in.  water),   to 7 cuft/cuft of  solid transferred.
                blowers  raise  to  Uess  than  40psig,  and  compressors  to  higher
                pressures,  although the blower range commonly is included in
                the compressor range.                           COOLING TOWERS
             2.  Vacuum pumps: reciprocating piston type decrease the pressure   1.  Water in  contact with air under  adiabatic conditions eventually
                to  1Torr; rotary  piston  down  to  0.001Torr,  two-lobe rotary   cools to the wet bulb temperature.
                down  to  0.0001Torr;  steam  jet  ejectors,  one  stage  down  to   2.  In commercial units, 90% of  saturation of  the air is feasible.
                100Torr.  three  stage  down  to  ITorr,  five  stage  down  to   3.  Relative cooling tower size is sensitive to the dilference between
                0.05 Torr.                                        the exit and wet bulb temperatures:
             3.  A  three-stage  ejector  needs  lOOlb steam/lb  air to  maintain a
                pressure of  1 Torr.                                        AT ("F)      5    75   25
             4.  In-leakage  of  air  to  evacuated  equipment  depends  on  the   Relative volume   2.4   1.0   0.55
                absolute pressure,  Torr,  and the volume of  the equipment,  V   4.  Tower fill is of  a highly open structure so as to minimize pressure
                cuft, according to w = kVZ3 lb/hr, with k = 0.2 when P is more   drop, which is in standard practice a maximum of  2in. of  water.
                than 90 Torr, 0.08; between 3 and 20 Torr, and 0.025 at less than   5. Water  circulation  rate  is  1-4gpm/sqft  and  air  rates  are
                1 Tors.                                           1300-1800 lb/(hr)(sqft) or 300-400  ftlmin.
                                             I  .\
             5.  Theoretical  adiabatic  horseDower  (THP) = T(SCFM)T, /8130al   6.  Chimney-assisted  natural  draft  towers  are  of  hyperboloidal
                                         ~           I  A.
                [(F''/P1)'  - 11,  where  TI  is  inlet  temperature  in  "F + 460  and   shapes because they have greater strength for a given thickness;
                a = (k - I)/k? k = C,/C,.                         a tower 250 ft high has concrete walls 5-6  in. thick. The enlarged
             6. Outlet temperature T, = G(P,/PJ.                  cross section at the top aids in dispersion of  exit humid air into
             7. To  compress  air  from  100"F,  k = 1.4,  compression ratio = 3,   the atmosphere.
               theoretical  power  required = 62 HP/million  cuft/day,  outlet   7. Countercurrent  induced  draft  towers  are the  most  common in
               temperature 306°F.                                 process industries. They are able to cool water within 2°F of  the
             8.  Exit  temperature  should  not  exceed 350-400°F;  for  diatomic   wet bulb.
               gases (C,,/C,  = 1.4) this corresponds to a compression ratio of   8.  Evaporation  losses are  1% of  the  circulation for every  10°F of
               about 4.                                           cooling range. Windage or drift losses of  mechanical draft towers
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