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440                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological



                       TABLE 14.4
                       Examples of Pre-Coat and Body-Feed Masses, Volumes, Concentrations
                                                            Pre-Coat                  Body Feed
                                    Plant Capacity
                                                   Mass   Volume   C(slurry) PC  Mass  Volume  C(slurry) BF
                                                                                                   3
                                                                        3
                       Plant      (mL=day)  (mgd)   (kg)    (L)     (kg=m )   (kg)     (L)     (kg=m )
                       Las Virgines  56.78   15    136.4    946      144
                       Hearst Castle                                           9.09     378     24.0
                       Mills        75.70    20    159     1325      120
                       Saratoga     15.14    4                                11.36    1,250     9.1
                       Rawlins      32.55    8.6   273     1136      240      136     11,355    12.0




            The velocity range for a DE slurry is 1.0   v(pipe)   1.83 m=s  point, for example, Microdact, with recording by computer
            (3.5   v(pipe)   6ft=s).                           software (the signal is calibrated by an instrument reading
                                                               and the instrument is calibrated to a standard at a specified
            14.3.1.2.3  Pumps                                  frequency).
            For pre-coat, a centrifugal pump may be used since a simple
            circulation is all that is required; in addition, the water flow  14.3.1.2.5  Control System
            from a centrifugal pump may be stopped by a valve without  To control the flows, actuated valves have been available
            building up excess pressure. The duration of the pre-coat step  since the 1980s along with pumps controlled by micro-relays
            is about 15 min. To use one volume change per min for the  (Mirliss, 2002, p. 14). The actuated valves and the pumps may
            slurry tank gives a pump size, Q(pre-coat) ¼ V(pre-coat)=  be set to operate based on signal levels, that is, pressure, time,
            (1 min). The headloss will be due only to the plumbing  turbidity, etc., that may be set by the operator using the
            configuration initially (which probably is negligible) but will  software, for example, Wonderwaret.
            rise to the pre-coat headloss at the end of the cycle, for
            example, 10–20 kPa (2–4 psi), depending on the grade of  14.3.1.3  Layout
            diaomite. The power required will be determined as  Figure 14.13 is an illustrative layout showing a module of
                                                               four DE tanks. The point is that through proper pipe layout
                P(pre-coat pump) ¼ Q(pre-coat)   g   h L (pre-coat)  and the use of an adequate number of ball valves, about any
                                            w
                                                       (14:10)  configuration is possible. Whatever the configuration, its logic
                                                               should be self-evident. The system should have  two mod-
            where                                              ules for redundancy with each module having  2 tanks. For
              P(pre-coat pump) is the power required to circulate pre-  small systems, however, a module may be one tank, with a
                coat (watts)                                   minimum of two modules. The backwash system is not shown
                                                   3
              g w is the specific weight of water (9808 N=m )   in Figure 14.13, but is depicted in Figure 14.2c.
              h L (pre-coat) is the headloss of pre-coat circulation flow  The floor area needed is the sum of the areas used by
                when pre-coat is deposited (m water)           each module (e.g., two tanks per module, four tanks per
                                                               module, etc.). Other kinds of functions requiring floor area
            For body feed, a positive displacement pump is recom-  include
            mended, for example, a positive displacement rotary progres-
            sive cavity pump (e.g., a Moynot) will avoid pressure pulses.  . A dock area for receiving bagged diatomite and other
            The motor should be direct current in order to provide for  materials
            variable body-feed flow.                               . A storage area for bagged diatomite
              For the raw-water pump, a rotary screw (progressive cav-  . A transfer area for breaking bags and transfer of
            ity) pump may be used if the flows are not too high, since the  diatomite to a slurry tank (the transfer area should
            flow is constant for a given motor rotation velocity. A direct  be designed to alleviate any problems of DE dust)
            current motor permits the raw-water flow to be adjusted from  . A bin, for storage of spent DE
            one run to the next.                                  . Outside storage for weeks or months accumulation
                                                                    of spent DE
            14.3.1.2.4  Instruments                               .  A laboratory for bench instruments and any wet
            Flow meters, pressure gages, temperature sensors, turbidity  chemical analyses deemed advisable and for calibra-
            meters, and perhaps on-line particle counters are required for  tions of on-line instruments
            operation. Each instrument category is available as an analog  . An office for administrative tasks (computer for
            sensor (i.e., 4–20 mA) that can be attached to an interface  reports to regulatory agency, storing data, etc.)
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