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CHEMICALS AND CHEMICAL HANDLING           '15.'13


         ride (CPVC),  3-in. (80-ram)  diameter,  as a precaution. Plug, needle-and-ball valves, 150-
         lb integral flanges with PVC or type 316  stainless steel construction, and tetrafluoroeth-
         ylene (TFE) or similar material sleeves  or retaining rings are recommended. A schematic
         layout of an alum feed system is shown in Figure 15.3.
           Caustic Soda Storage.  Liquid caustic soda  is delivered by railcar and tanker truck.
         Tanker trucks can haul up to 3,000 gal (11,400  L) per load.  Storage  tanks should be con-
         structed of stainless steel, FRP, polyethylene, or steel lined with rubber or polypropylene.
        As with alum, schedule-80 PVC with socket  end joints is the recommended piping ma-
        terial if liquid temperatures  do not exceed  120 ° F  (49 ° C).  Caustic soda  generates heat
        when mixed with water, resulting in temperatures approaching this level, so use of CPVC
        piping should be considered for this application. Valves can be steel  or ductile iron with
        Teflon components, rubber-lined, or PVC.
           The freezing point of caustic soda solution is highly dependent on the solution strength
        (Figure 15.4). Freezing points for solutions greater  than 50%  quickly elevate,  making it
        impractical to  handle and store.  Because  50%  caustic soda begins to  crystallize at  ap-
        proximately 54 ° F (12 ° C), storage tanks must be indoors or insulated and heated to avoid
        crystallization.  A typical chemical feed schematic for caustic soda appears  in Figure 15.5.
           Sodium Hypochlorite  Storage.  Commercial sodium hypochlorite (NaOC1), or liquid
        bleach, is marketed in carboys and rubber-lined drums holding up to 50-gal (190-L)  vol-
        ume, and in trucks.  Storage  tanks should be constructed of FRP, polyethylene, or steel
        lined with rubber or polypropylene. As with alum, schedule-80 PVC with socket end joints
        is the recommended piping material if liquid temperatures  do not exceed 120 ° F (49 ° C).
           Valves may be a plug type made of steel  (lined with PVC or polypropylene), or PVC
        diaphragm valves. Although PVC ball valves would not react with the chemical, hypochlo-
        rite releases  small amounts of gas  as it decomposes,  and PVC ball valve failures due to
        gas buildup have been reported.  A similar type of failure has occurred with stainless steel
        (SST) ball valves in hydrogen peroxide service.  Any type of ball valve, especially 1-in.
        and larger sizes, may allow hypochlorite to weep through the seal and crystallize.  To avoid
        these  problems, a diaphragm valve constructed of composite material using a Teflon di-
        aphragm can be used.
           When hypochlorite is added to water, it hydrolyzes to form hypochlorous acid (HOC1),
        the same active ingredient that occurs  when chlorine gas is used.  The hypochlorite reac-
        tion slightly increases the hydroxyl ions (pH  increase) by the  formation of sodium hy-
        droxide,  whereas  the reaction of chlorine gas with water increases the hydrogen ion con-
        centration (pH decrease),  forming hydrochloric acid. In most waters, these differences are
        not significant, but when high chlorine doses  are used in poorly buffered waters,  these ef-
        fects  should be considered.  They can be evaluated by calculation or by simple laboratory
         tests.
           In the commercial trade, the concentration of sodium hypochlorite solutions is usually
         expressed  as a percentage.  The trade percent is actually a measure of weight per unit vol-
         ume, with 1% corresponding to a weight of 10 g of available chlorine per liter. Common
         household bleach, at a trade concentration of 5.25%,  has approximately 5,25  g/100 mL
         or 52.5 g/L of available chlorine. Hypochlorite available for municipal use usually has a
         trade  concentration of  12.5% to  17%. These are  approximate concentrations and should
         always be confirmed by laboratory procedures.
           Because increasing the concentration of any salt lowers the freezing point of a solu-
         tion, the freezing points of various solutions of sodium hypochlorite are a function of their
         concentrations, with the more dilute concentrations approaching the freezing point of pure
         water. Figure 15.6 shows the freezing temperature of hypochlorite solutions as a function
         of concentration in the concentration ranges normally experienced.
           The chlorine concentration in hypochlorite solutions is adversely affected by high tem-
         perature,  light,  low pH,  and the  presence of certain heavy metal cations. Iron, copper,
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