Page 302 - APPLIED PROCESS DESIGN FOR CHEMICAL AND PETROCHEMICAL PLANTS, Volume 1, 3rd Edition
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272                       Applied Process Design for Chemical and Petrochemical Plants

                                                                     LIQUID  LI.V£L

                                        D'- Clean gas out









                                                                  LDW PIU!SSURE
                                                                  l)flOP V£NTURI  ___..#//             FLEXITRAV
                                                                                   �
                                                                  li.NTllY      ,J � q9
                                                                                          1
                                                                Figure 4-64A.  Adjustable "floating" caps for vapor flow.  By permis-
                                                                sion,  Koch Engineering Co.,  Inc.









          Gas plus
          suspended
          solids In
           +A>
              �












                                                                                         DUST
                                                                                        STORAGE
                                                                                         HOPPER
                                                                            FILTERING              CLEAN I  NG
          The scrubber is comprised of one or more trays.  Each tray contains
          numerous  venturi  openings.  Each  of the  MultiVenturi  openings  is   Figure 4-65. Bag filtration with mechanical shaking for bag cleaning.
          surmounted by a spider cage holding a floating Flexicap (see insert).   Courtesy of Dracco Div.  Fuller Co.
          In addition,  each tray  Is equipped with one or more  "downcomers"
          and  weir flow  baffles  that  control  the  scrubbing  liquid  as  it flows
          across the tray and then to the tray below.
                                                                dust  loading  [ 47]. The air-to-cloth  ratio  so  often  used  is
          Figure  4-64.  Variable  orifice  MultiVenturi  Flexitray®  scrubber  at   only  useful when  comparing a  particular manufacturer's
          essentially constant pressure  drop  maintains good  efficiency  over   equipment for handling different materials,  and  not for
          wide flow rates.  By permission,  Koch Engineering Co., Inc.   comparing manufacturers.  Reference  [ 49]  is an excellent
                                                                summary  of many  details  associated  with  specifying  and
                                                                selecting bag filters.
          bag by internal arrangements in the "bag house" or hous-   The following are  suggested filter specifications:
          ing by such techniques as  (1)  shaking or vibrating the bag
          or bag assembly  to drop the dust into an integral  hopper   l. Performance:  define air  /gas and dust rates,  particle
          while there is no-flow of air-dust feed into the unit or com-   size distribution, and percent of particle sizes.
          partment,  or  (2)  back  pulse with jets  of air in to each bag
          (Figure 4-67). The criterion should be a constant pressure   a. Temperature at inlet to baghouse
          drop across  the fabric for a fixed air flow and a  specified   b.  Moisture concentration, dewpoint
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