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10-16   WATER AND WASTEWATER ENGINEERING

                                            ws

                             Height of interface  H  HS  HS  TS



                                                    TS
                                            TS
                                            TS
                                            CS      CS     CS      CS
                                    t   0   t   t 1  t   t 2  t   t 3  t   t 4
                            (a)

                                     Slope   settling
                                       velocity        Hindered (zone)
                             Height of interface       settling (HS)




                                                       Transition settling (TS)
                                                       Compression settling (CS)
                                     t 1  t 2   t 3  t 4
                            (b)          Time
                              FIGURE 10-11
                               Idealized schematic of Type III and IV settling in a column ( a ) and
                            a graph of the corresponding settling curve ( b ).   ( Source:  Metcalf
                            and Eddy, 2003.)


                              hindered  settling. The rate of hindered settling is a function of the concentration of the particles
                            and their characteristics.
                                As settling continues, a compressed layer of particles begins to form. The particles are in
                            contact and do not really settle. A more correct way to visualize the phenomena is the flow of
                            water out of a mat of particles that is being compressed. Thus, it is called  compression  settling.
                                As with Type II settling, the methods for analyzing hindered settling require settling test
                            data. These methods are appropriate for plant expansions or modifications but have not found
                            use in the design of small treatment plants. The methods are described in detail in Chapters 15
                            and 25.

                              High-Rate Settling.  Increasing the particle density, or reducing the distance a particle must fall
                            prior to removal, can accelerate the clarification process.
                                 The specific gravity of alum floc is approximately 1.001 and that of lime floc is 1.002
                            (Kawamura, 2000). Several proprietary processes add a ballast (usually microsized sand 20 to
                            200    m diameter) with a specific gravity on the order of 2.5 to 2.65 to the floc to increase its set-
                            tling velocity. The sand is recovered and reused.
                                 To reduce the distance the particle must fall, a series of inclined plates or tubes are placed in a
                                                                                                            .
                            rectangular horizontal flow settling basin. Three typical configurations are shown in  Figure 10-12
                            The plates or tubes are inclined to a degree that allows the collected solids to slide down the sur-
                            face to the sludge zone. Typically the tube is a square, about 5 cm on each side, and the angle is
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