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Disinfection                                                                                     631


                                                               Ozone
                                    Reactor
                                                              generator
                               P         N  = 1000 #/L       (6 element)  Air       Air preparation
                                          0


                            Water flow

                         Ozone bubbles                                                 Dessication
                             Diffusers           Ozone
                                                                                       After-cooler

                         Ozone bubbles
                             Diffusers           Ozone                                 Compressor





                                              N= 1 #/L

            FIGURE 19.9  Schematic drawing of an ozone system, 0.84 kg O 3 =day, u(reactor) ¼ 21 min, CSU pilot plant.


            that acts as a second electrode. Feed gas flows within the  19.4.5 UV REACTORS
            space between the outer and inner tube, that is, the ‘‘discharge
                                                               Factors in the UV reactor design include (Malley, 2000, p. 8;
            gap.’’ The power required depends upon the oxygen content
                                                               Malley, 2002b, p. 2): number and type of UV lamps used; UV
            of the feed gas and the ozone concentration of the product
                                                               reactor hydraulics; level of inactivation required; location of
            gas. For a 1% ozone concentration, about 7.5–8 kWh are
                                                               UV in the treatment train; degree of redundancy desired;
            required to generate 0.5 kg O 3 (1 lb), for example, about
                                                               water quality characteristics that result in UV attenuation;
            16 kWh=kg O 3 .
                                                               minimum temperature for lamp operation; degree of lamp
              Once the ozone is produced, it must be transferred to the
                                                               fouling by inorganic constituents such as hardness and iron;
            water in the reactor, which requires a diffuser (see Chapter 18).
                                                               fouling by organics; number and type of UV sensors; reactor
            Although a variety of diffusers have been used, a fine bubble
                                                               geometry; reactor material; provision for cleaning lamps;
            diffuser set up in the counter-current mode in a pressure vessel
                                                               instrumentation; and controls. Low-pressure UV lamps, with
            reactor is most efficient.
                                                               operating temperature range, 408C < T < 608C, may have
              The Henry’s constant for ozone is H(O 3 ,208C) ¼ 482 mg
                                                               unstable output at low water temperatures, for example,
            O 3 =L water=atm O 3 , which is about 10 times higher solubility
                                                               0.58C. Medium-pressure lamps operate at 4008C < T < 6008C;
            than oxygen. Once dissolved in water, the next task is to
                                                               low water temperature is not an issue (Malley, 2000, p. 11).
            facilitate the contact between the ozone and other reactants,
            for example, microorganisms in the case of disinfection,
            and to provide sufficient detention time, u, such that the  19.4.5.1  Hydraulics
            needed Ct(target microorganism) is satisfied. Due to hydraulic  UV reactors are designed as ‘‘plug flow’’ (vis a vis complete
            dispersion, the organisms in the effluent flow will have a  mix). As noted in Section 4.3.3.3, the hypothetical ‘‘plug
            range of Ct’s.                                     flow’’ may be approximated most closely to a reactor that is
                                                               long relative to its cross section. At the same time, turbulence
                                                               is necessary in order to provide lateral dispersion; the idea is
            19.4.4 CHLORINE DIOXIDES                           to expose a very large fraction of the organisms to ‘‘killing’’
            Chlorine dioxide is generated onsite also (i.e., as is ozone)  levels of UV doses during their irregular, that is, random,
            using proprietary equipment (see, for example CDG  longitudinal flow paths.
            Environmental, Bethlehem, Pennsylvania). In water treatment
            practice, chlorine-dioxide concentrate solutions are usually  19.4.5.2  UV Reactors Volume
             4000 mg=L (Aieta and Berg, 1986, p. 62). The concentrate  A UV reactor is a specified volume that can accommodate one
            must be diffused throughout the reactor, for example, by a jet-  or more ‘‘banks’’ of UV lamps and which results in the needed
            mixer. The reactor should be of the ‘‘plug flow’’ type, with the  Ct’s for a specified log R. Due to the variation in the ‘‘resi-
            detention time based on the Ct parameter. Because of  dence times,’’ that is, from hydraulic dispersion,’’ the log R
            hydraulic dispersion, the average detention time, u, should  should be that achieved for a particular fraction of the sam-
            be such that the calculated, Cu   Ct(target organism), that is,  ples, for example, log R(0.99 fraction of samples)   3. A UV
            due to the variation in residence times in the reactor (as seen  reactor may be a section of a pipe, or an open channel. The
            by a tracer).                                      former is found more commonly in drinking water treatment
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