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CHEMICAL HANDLING AND STORAGE 5-9

             TABLE 5-2
            Dry feeder characteristics
                                                                  Capacity       Turn-down
                                                                     3
          Type of feeder     Application                            m /h            ratio   Remarks
          Gravimetric
                                                                       4
           Loss-in-weight    Granules, powder or lumps           6   10  to 2      100:1
                                                                      4
           Continuous belt   Dry, free-flowing granules        6   10  to 0.06     100:1    Use hopper agitator
                                                                                            to maintain constant
                                                                                            density
          Volumetric
                                                                       4
           Rotating disc     Dry, free-flowing granules or powder  3   10  to 1     20:1    Use disk unloader for
                                                                                             arching
           Rotating cylinder  Dry, free-flowing granules or powder  0.2 to 60       10:1
                                                                       3
           Screw             Dry, free-flowing granules or powder  1   10   to 1    20:1
                                                                        5
           Ribbon            Granules, powder or lumps           6   10  to         10:1
                                                                         3
                                                                  5   10
                                                                      3
           Belt              Dry, free-flowing granules or powder   3   10   to 85  10:1
                             up to 3 cm size
           Adapted from Hudson, 1981, and Kawamura, 2000.

             The characteristics of dry chemical feeders are summarized in  Table 5-2  .



            Gravimetric Feeders.  There are two types: loss-in-weight and belt-type. The loss-in-weight
          type uses a feed hopper suspended from scale levers, a material feed control mechanism, and
          a scale beam with a motorized counterpoise. The rate of weight loss of the hopper equals the
          weight loss equivalent of a traveling counterpoise when the feeder is in balance. If it does not, the
          scale beam deflects and the feed mechanism adjusts the feed rate.
               A feed hopper and control gate regulate the flow and depth of material on the belt-type
          feeder. A scale counterpoise is adjusted to establish the desired belt loading. The gate releasing
          material and the speed of the belt are adjusted to produce the desired flow of material.
               The loss-in-weight type feeder capacity is limited to about 400–500 kg/h. The belt-type feeders
          have capacities of 225 Mg/h and up.


            Volumetric Feeders.  The volumetric feeders provide good overall performance at low feed
          rates and acceptable accuracy for materials with stable density and uniformity. They do not per-
          form well when the density of the material is not stable or is hygroscopic. They must be cali-
          brated frequently.


            Lime Slakers.   Slaking  means combining water with  quicklime  (CaO) in various proportions to
          produce milk of lime or a lime slurry. Lime feed systems combine the addition of the chemical
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