Page 231 - Fluid mechanics, heat transfer, and mass transfer
P. 231

TWO-PHASE FLOW    209
            TABLE 7.2  Materials Transported by Pneumatic Conveyance

            ABS powder            Acetyl salicylic acid   Adipic acid                Activated earth      Alumina
            Ammonium sulfate      Ammonium nitrate        Granulated cattle feed     Anthracite           Cement
            Bagasse fines          Cellulose acetate       Charcoal granules          Chalk                Clays
            Ground coffee         Coke dust               Bleaching powder           Cotton seeds         Copra
            Calcium chloride      Limestone               Magnesia                   Flour                Bran
            Milk powder           Glass fibers             Nitrocellulose             Sawdust              Soot
            Graphite powder       Gypsum                  Paper mill wood waste      Peanut shells        Starch
            Phthalic anhydride    Plaster                 Polyethylene granules      Granulated sugar     Sulfur
            Polystyrene beads     Polyester fibers         PVC powder and granules    Sodium sulfate       Talc
            Terephthalic acid     Titanium dioxide        Soap flakes                 Silica gel           Yeast
            Sodium carbonate      Zinc oxide              Wood shavings              Tobacco              Fly ash



              . Give a list of some materials conveyed by pneumatic  & Minimum conveying velocity is a function of flow
                conveyance.                                            rate.
                & Table 7.2 provides a list of materials that are con-  & Relative humidity of conveying air should be more
                  veyed by pneumatic conveyance.                       than 70%, to avoid electrostatic effects.
              . What are the important guidelines with respect to  . What are the characteristics of particulates that are
                selection, specification, and design of pneumatic con-  handled by pneumatic conveying?
                veyance systems?                                     & Pneumatic conveying can be used for particles rang-
                & During the project stage, current conveying rate     ing from fine powders to pellets with bulk densities of
                                                                                  3
                                                                                             3
                  requirements and plant layout along with plans for   16–3200 kg/m (1–200 lb/ft ).
                  future expansions or potential rate enhancements due  & Among the important particle characteristics are
                  to improvements in process technologies need to be   particle size and size distribution, shape, density,
                  considered.                                          hardness, and friability.
                & Minimum and maximum conveying rates should be        ➢ Particle size, distribution, and shape are known to
                  carefully defined.                                      be among the most significant variables affecting
                & A reasonable horizontal conveying length (15–20        pneumatic conveying. For example, uniformly
                  pipe diameters), with minimum flexible hose length,     sized round and smooth particles are easier to
                  should be allowed before the first bend to allow the    convey than angular, rough ones having a wide
                  bulk material to accelerate.                           size distribution.
                & Placing bends/elbows back to back in the line should  ➢ Another rule of thumb is that, to prevent mechan-
                  be avoided. The number of bends should be kept to      ical plugging of conveying lines, particularly
                  minimum.                                               when conveying materials containing large parti-
                                                                         cles, the pipe diameter must be at least three to five
                & Pipe diameter should be increased at the end of the
                                                                         times the maximum particle dimension.
                  line to prevent excessive velocity and reentrainment
                  of the particulates.                                 ➢ Particle density affects the minimum conveying
                                                                         velocity and pressure drop required for transport.
                & Proper venting of the rotary air lock and feeder in a
                  positive pressure system is critical for reliable  & Bulk properties that are important include bulk den-
                  operation. Gas leakage at feeder must be consid-     sity and compressibility, permeability, cohesive
                  ered in design calculations and adequately           strength, segregation tendency, explosibility, toxici-
                  compensated.                                         ty, reactivity, and electrostatic effects.
                & The gas flow control system for multiproduct and      ➢ The compressibility and permeability of a bulk
                  multidestination systems must ensure that the oper-    solid determine how readily the material will
                  ating point is maintained within the stable operating  deaerate.
                  zone.                                                ➢ The direct effect of the cohesiveness of a bulk solid
                & It must be noted that product damage and wear at pipe  on pneumatic conveying can be buildup in the
                  bends depend on the nature of the material.            lines. Flow stoppages, or erratic flow through
                                                                         equipment upstream of a conveying line, such as
                & A proper purge control sequence need to be de-
                                                                         in a bin, feeder, or chute, can be detrimental to
                  signed and tested to avoid product degradation or
                                                                         achieving the desired transfer rates.
                  blockage.
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