Page 283 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
P. 283

Mechanical Separations                                     255



















                             - particle-laden  gas
       Materials of construction
       Packing of York-Fiberbed high efficiency mist eliminators consists of
       ceramic,  glass,  polypropylene, fluoropolymer  fibers.  Cages  and
       frames are fabricated from all stainless steels and other weldable
       alloys as well as FRI?

       Figure 4-27A. Details of a cylindrical York-Fiberbed@ mist eliminator.
       Courtesy of Otto H. York Co., Inc., Bullet in 55B.


        particle  size  removed  may  be  much  smaller. Just  as for
        other types of mist eliminators, the performance is affect-
        ed by the properties of the liquid particles, entraining gas,
        temperature, pressure, liquid viscosity, particle size distri-
       bution  of  entrained  material  and  the  quantity  of  total
       entrainment,  and  the  desired  process removal  require-
       ment. Some designs of these units provide excellent per-
       formance  removal efficiencies at a wide  range  of  rates
        (turndown), even at low gas rates.
          Pressure drop is  usually low depending on many fac-
        tors, but can be expected in the range of 2 to 20 inches of
       water [33].


       Baffle Type Impingement

          There are  many baffle type  impingement separators.   Figure 4-278.  Fiber-pack@ mist eliminator pack separators. By per-
       The efficiency of operation for entrainment is entirely a   mission, Koch Engineering Co., Inc. Note that other manufacturers
       function  of  the  contacting  action  inside  the  particular   have  basically the  same  concept;  however, the  identification of
       unit. There are no general performance equations which   types are peculiar to each.
       will  predict performance for this type of unit; therefore
       manufacturers’ performance data and recommendations   liquid droplets run down on the plate surfaces counter-
       should  be  used.  A  few  of  the  many  available units  are   current to the up-flowing gas stream. See Reference [59]
       shown in Figures 428 to 431. Many use the Chevron-style   for performance study.
       vertical plates as shown in Figures 417A and 430.        Spacing of  the plates and their  angles is a part  of  the
                                                             design using the manufacturers’ data. Multiple pass designs
        Baffles (Chmons/Vanes)                               can result in higher recovery efficiencies. The units can be
                                                             designed/installed for vertical or horizontal flow.
          One of the common impingement plate assemblies is     Some of the same physical properties of the liquid and
       of the Chevron  “zig-zag” style of Figures 417A and 430.   gas phases as well as temperature  and pressure  and the
       This style of impact separation device will tolerate higher   amount of entrained liquids (or solids if present) and the
       gas velocities, high liquid loading, viscous liquids, reason-   expected  particle  size  and  its  distribution  control  the
       able solids, relatively low  pressure  drops.  The collected   design and performance of these units also.
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