Page 425 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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380                            Fundamentals of Water Treatment Unit Processes: Physical, Chemical, and Biological
























            FIGURE 12.45  Culligan Multi-Techt filtration system as set up at
            Colorado State University, 1985, for evaluation of removals of Giar-
            dia cysts. (Courtesy of ABWt Infilco-Degremont, Richmond, VA.)
                                                               FIGURE 12.46 Automatic backwash (ABWt Infilco-Dregemont)
                                                               at Ignacio, Colorado.

                                                      2    2
            Concrete modules have been constructed up to 4.65 m (50 ft ).
                                                               to a filtered water flume on one side that runs the length of the
            Parkson listed some 300 installations for industrial water and
                                                               filter giving a common tailwater elevation for all cells. Back-
            wastewater treatment (Parkson DS1, 1991).
                                                               wash is accomplished by a traveling bridge that has a backwash
                                                               pump and a ‘‘shoe’’ that fits over the under-drain block for a
            12.8.2.2  Deep Bed Filtration—Culligan Multi-Techt
                                                               particular cell during the time of backwash. The backwash
            The Culligan Multi-Techt came about from the collaboration  water source is the flume of finished water. The bridge moves
            with Professor E. Robert Baumann (Iowa State University)  continuously from one cell to the next and from one end of the
            and John Scanlan (Culligan) in the early 1980s. The system  bed to the other and back. Figure 12.46 shows an ABWt
            was intended for small municipal water systems as a package  system as installed for municipal water treatment at Ignacio,
            technology, made feasible by modern SCADA systems (the  Colorado. The system has been used for filtration of secondary
            Culligan had a form of this by the mid-1980s). Figure 12.45 is  treated wastewater. An example is at Aspen, Colorado,
            a photograph of a system, c. 1985, which was effective in  where such a filter is used following secondary biological
            reducing turbidity to low levels and in removing Giardia  treatment and before discharge of the effluent into the Roaring
            lamblia cysts (Horn et al., 1986; Horn et al., 1988). The key  Fork River.
            components are: a centrifugal pump that pressurizes a system,
            a first stage filter of coarse media, and a second stage filter of  12.8.2.4  Package Filtration—EPD Wearnes USAt
            graded media, finer than in the first stage. The coagulant is  The EPD Wearnes USAt filter system started as a swimming
            injected into the first stage. Backwash may be programmed on  pool filter in the 1980s (under its predecessor company Envir-
            time, on headloss, or turbidity breakthrough. The coagulant  onmental Products Division, Hoffinger Industries) and then, in
            dosage must be determined by the operator.         the early 1990s, after further development, found a market in
                                                               small drinking water system applications. The filter system is
            12.8.2.3  Shallow Bed Filtration—ABWt              two stage, each stage in a cylindrical tank with horizontal axes.
            The automatic back wash filtration system (ABWt) was  The two tanks are filled with media of garnet to a depth of 305
            developed in the 1950s by Hardinge and was later acquired  mm (12 in.) with the first stage coarser than the second. For the
            by Environmental Elements, Inc. of Baltimore, later assimi-  first unit, d 10 ¼ 0.27 mm, UC ¼ 1.6, and for the second unit
            lated by Infilco-Dregremont, Inc. (http:==www.degremont-  d 10 ¼ 0.18 mm, UC ¼ 1.3. The backwash rate was 37 m=h
                                                                        2
            technologies.com=dgtech.php?article390). The filter has had  (15 gpm=ft ) without loss of media. The system is automated
            skeptics due to its shallow depth and ostensibly short duration  and is backwashed based on pressure, time, or effluent turbidity.
            backwash. Despite this the system has been adopted rather  Coagulant feed and turbidity and particle counting instrumenta-
            widely for both municipal drinking water and for filtration of  tion were a part of the ‘‘package,’’ along with a SCADA system.
            secondary effluent from biological wastewater treatment. The
            bed may be 30 m (100 ft) long   6.1 m (20 in.) wide and is
                                                               12.8.3 EVALUATION OF PRODUCTS
            divided into cells about 305 mm (12 in.) wide with plastic
            partitions. The headwater is the same for all cells and thus the  Information on virtually any product is available through
            filtration scheme is ‘‘declining rate.’’ The under-drain for a  various sources, for example, manufacturer’s brochures,
            given cell collects water from that cell only with conveyance  Web sites, and manufacturer’s representatives. Trade shows
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