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230                       Applied Process Design for Chemical  and Petrochemical  Plants
                                                       99.99---.---...-  ...... �.,..,.--.,.........,.--,-,....,-i��---,�...,......,  ...   O.Ql
                                                                                                 (o,.,           0.05
                                                       99.9                                        .. l!>;z.     0.1
                                                       99.8                                        "-,/��  'JC),   0.2
                                                                                                         C),C'/,   0.5
                                                       99.0                                                o,,&   1.0
                                                       95.0                                                      5.0
                                                       90.0                                                     10.0  '*'
                                                                                                                    ii'
                                                                                                                20.0  c:  .,
                                                                                                                    ·.;
                                                                                                                    ..
                                                                                                                    i:
                                                                                                                50.0  c:
                                                                                                                    .2
                                                                                                                    t,
                                                                                                                    �
                                                                                                                    0
                                                       20.0                                                         o
                                                       10.0                                                     90.0
                                                        5.0                                                     95.0
                                                        1.0                                                     99.0
                                                        0.5
                                                        0.2
             Figure  4-4.  Comparison  chart showing  ranges  of   0.1                                          99.8
                                                                                                                99.9
             periormance of several collection/control  devices   0.05
             in  air  streams.  By  permission,  Vandegrift,  et.  al.   O.Ql  ..__  .....  _.._..._.._.....,.w..  __  _.._.._..._..._A,.., .....  ..._   ..._  _  _.  99.99
             Chemical Engineering,  Deskbook  Issue,  June  18,   0.01        0.1                1.0
             1973,  p.  1 09.                                                Particle diameter, microns

                (b)  Spherical  particles  between  100 and  1500 microns   (d)  Spherical  particles  between  0.1  and  3  microns:
                   diameter [BJ:                                         Stokes-Cunningham  Law  [12]:

                                                                     u.  = .K,,,urs                              (4-6)
                     o.J53g/·710/14  (p,  -  p)o.1
                l1  l  =                                   (4-4)
                             p  0.29µ 0.43                                                                       (4-7)
                          -06
                C =  18.5  NRc   ·   ,  (See Figure 4-1)                                                         (4-8)

                                                                     This represents a  correction on Stokes Law and is  sig-
                (c)  For spherical  particles between 3  and  100 microns   nificant for 3  micron  and smaller particles  in  gases  and
                   and  Reynolds  numbers  between  0.0001  and  2.0,   0.01  micron  and  smaller  particles  in  liquids.  Table  4-8
                   Stokes Law:                                     gives values of K,,,.

                                                                     When  two  free  settling  particles  of different  climen-
                CNRe  =  24                                        sions,  D'  pl  and  D'  P 2   and  different densities,   Ppl  and   Pp2,
                                                                   fall  through  a  fluid  of density,  Pr,  they  will  attain  equal
                                                                   velocities when:


             and:
                                                                                                                (4-9)


                                                           (4-5)   where n  =  1  in eddy-resistance zone (more turbulent)  and n  =
                                                                            0.5 in streamline fall.

                                                                   Alternate Terminal Velocity  Calculation
             for  particles  smaller  than  0.1µ  the  random  Brownian
             motion is greater than the motion due to gravitational set-   In  contrast  to  individual  particles  settling  in  a  very
             tling.  Therefore  the above  relations based on Stokes Law   dilute  solution/fluid,  is  the case  of sedimentation where
             will not hold.                                        particles  must settle in more concentrated  environment,
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