Page 255 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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Mechanical  Separations                                    225

                                Table 4-1                                             Table 4-3
                    Sizes  of Common Dusts and Mists                           Dry Particle Screen Sizes
                                        Average  Particle Diameter,   W. S. Tyler Screen
            Dust  or  Mist                     Microns                Scale                       Micron  (approximate)
            Human  Hair  (for comparison) ....   50-200                 80   ·  ·  ·  ·  ·  ·  ·  ·  ·  ·  ·  -  ·  ·  ·  ·  ·. ·  ·   -   174
            Limit of visibility with  naked eye ..   10-40              100   ..................................  146
            Dusts                                                       115   ..................................  123
             Atmospheric  dust        .          0.5                    150   .............................•....  104
             Aluminum                 .          2.2                    170   .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .   89
             Anthracite  Coal  Mining                                   200   .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  . .  .  .  .  . .  .  .  •  .  .  .  .  .  .   74
               Breaker  air           .          1.0                    250   .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .   61
               Mine  Air              .          0.9                   270   .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  . .  .  . .  .  .  .  .  .  .   53
               Coal  Drilling         .          1.0                   325   .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .   43
               Coal  loading          .          0.8
               Rock  drilling         .          1.0
             Alkali  fume             .          1-5
             Ammonium  Chloride  fume   .     0.05-0.1-1                              Table 44
             Catalyst  (reformer)     .         0.5-50
             Cement                   .       0.5-40-55             Approximate  Particle Sizes  From Liquid  Full  Cone
             Coal                     .         5-10                                Spray  Nozzles*
             Ferro-manganese,  or  silicon   .   0.1-1
             Foundry  air             .          1.2                                Liquid:  Water
             Flour-mill               .          15
             Fly  Ash  (Boiler Flue  gas)   .   0.1-3
             Iron  (Gray  Iron  Cupola)   .    0.1-10                            Operating  Pressure,  Approx.  Mean  Particle
             Iron  oxide  (steel  open  hearth) ..   0.5-2       Nozzle  Size,  In.    Psig           Size,  Microns
             Lime  (Lime  Kiln)       .         1-50             ---y;----:-:-:-: . . . . . . . . . . .  15  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  1200
             Marble  cutting          .          1.5                                    60  .  .  .  .  .  .  .  .  .  .  .  .  .  .  .   750
             Pigments                 .         0.2-2                  %                10                1600
             Sandblasting             .          1.4                                    40                1000
             Silica                   .         1-10                      ...............  15             1750
             Smelter                  .        0.1-100                                  40                1250
             Taconite  Iron  ore                                      lYz               15               2300
               (Crushing  &  Screening)   .    0.5-100                                  60  .........•......  1800
             Talc                   ·  ·.        10                  3    .  .  .  .  .  .  .  .  .  .  .  .  .  .  .  10   5300
             Talc  Milling            .         l.5                                     30  .........•......  4300
             Tobacco  smoke           .         0.2
             Zinc  oxide  fume        .         0.05
             Zinc  (sprayed)          .          15              *Private  communication,  Spraying  Systems  Co.,  Bellwood,  Ill.
             Zinc  (condensed)        .          2
           Mists
             Atmospheric  fog         .         2-15             Example 4-1: Basic Separator Type Selection [2, 17]
             Sulfuric  acid           .        0.5-15
           Compiled from References  1,  13, and  15.               A  suitable  collector will  be  selected  for a  lime  kiln  Lo
                                                                 illustrate  the  use  of the Sylvan  Chart  (Figure  4-3). Refer-
                                                                 ring  to  the  chart,  the  concentration  and  mean  particle
                                Table 4-2                        size  of the  material  leaving  the  kiln  can  vary  between  3
                       Typical Dust Size Analysis-IC·            and  10 grains/  cu ft  with  5  to  10  microns  range  of mass
                                                                 mean  particle  size.  Assume  an  inlet concentration  of 7.5
                                         DUST                    grains/  cu  ft  and  inlet  mean  particle  size  of 9  microns.
                                  Cement             -----       Projection of this point vertically  downward  Lo  the collec-
                                    Kiln    Foundry
                          Rock    Exhaust    Sand   Limestone    tion efficiency portion of the chart will indicate that a low
                                                    -�--
         Sp.  Gravity     2.63    2.76      2.243      2.64      resistance  cyclone will  be  less  than  50%  efficient;  a  high
         Apbarent  we,                                           efficiency  centrifugal  will  be  between  60  and  80%  effi-
           1  s./cu.ft.  .  ....  61.3   52.0   45.9   72.0
         Screen  Analysis                                        cient,  and a wet collector,  fabric arrester and electro-stat-
           ( Percent  passed)                                    ic  precipitator will  be  97%-plus  efficient.  The  last three
           100  Mesh      98.8     99.6      91.2     85.6
           200  Mesh  .....  92.8   92.2     78.4     76.4       collectors  are  often  preceded  by  a  precleaner  so  a  high
           325  Mesh  .....  79.6   80.8     67.6     66.4       efficiency  centrifugal  will  be  selected.  Using  the  average
           400  Mesh  .....  70.8   73.2     64.4     63.2
         Elutriation  Analysis:                                  line of this  group,  the efficiency will be  70%.  Therefore,
           Percent  Under                                        the effluent from this collector will have a  concentration
           Terminal  Velocity                                    of 7.5(1.00  - 0.70)  =  2.25  grains/cu ft.
           320  In./min.   75.8    78.0      64.2     70.5
            80  In./min.  ..  37.0   61.0   53.9      52.0
            20  In./min .  .  .   17.5   40.8   42.0   33.0         Draw  a  line  through  the  initial  point with  a  slope par-
             5  In./min .  .  .   8.9   23.0   32.0   18.0       allel  to  the  lines  marked  "industrial  dust." Where  devia-
         -�------                                                tion is  not known,  the  average  of this  group  of lines  will
         *Compiled  from  Bulletin  No.  1128,  American  Blower  Corp.,
          Detroit,  Michigan.                                    normally be sufficiently accurate to predict the mean par-
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