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




                                      10 –1
                                      10 –2
                                      10 –3
                                      10 –4
                                      10 –5
                                      10 –6                                k S
                                    k ij  (cm 3 )  10 –7                       k SH
                                        –8
                                      10
                                      10 –9
                                      10 –10                                    k B
                                      10 –11
                                      10 –12
                                      10 –13
                                      10 –14
                                      10 –15
                                         10 –2    10 –1     10 0     10 1     10 2     10 3
                                  (a)                       Particle size (μm)
                                        10
                                      10 –1
                                      10 –2
                                      10 –3
                                                                                k SH
                                      10 –4
                                        –5
                                    k ij  (cm 3 /s)  10 –6                      k S
                                      10
                                        –7
                                      10
                                      10 –8
                                      10 –9
                                                                                   k B
                                      10 –10
                                      10 –11
                                      10 –12
                                         10 –2    10 –1     10 0     10 1     10 2     10 3
                                  (b)                      Particle size (μm)

            FIGURE 11.3 Effect of target particle size on collision rate constants for conditions indicated. (a) Settling basins. (b) Flocculation basins.
            (Adapted from O’Melia, C.R., Coagulation in wastewater treatment, in: Ives, K.J. (Ed.), The Scientific Basis of Flocculation, Sijthoff &
            Noordhoff International Publishers, Alphen aan den Rijn, the Netherlands, p. 228, 1978.)
              g is the acceleration of gravity ¼ 9.806650 m=s 2
              SG p is the specific gravity of solid particles (dimensionless)              Conditions
              n is the kinematic viscosity of water at temperature,  Parameter  Settling Tank    Flocculation Tank
                    2
                T (m =s)
                                                                 Tank        Settling               Flocculation
                                                                 Reference   O’Melia (1978, p. 228)
              Figure 11.3a and b shows how the three rate coefficients,
                                                                 Figure      11.3a                  11.3b
            i.e., k B (i, j), k SH (i, j), k S (i, j) vary with particle diameter for
                                                                 d i (mm)    1                      10
            the conditions of a settling tank and a flocculation basin,          2  2                  2  3
                                                                 d j (mm)    10 –10                 10 –10
            respectively. As seen in Figure 11.3a, Brownian motion is
                                                                 T (8C)      5                      20
            dominant for d(particle) < 10 mm but for d(particle) > 10 mm,
                                                                 SG          1.02                   1.02
            settling becomes dominant. For a flocculation basin, Figure
                                                                     1
                                                                 G (s )      0.1                    10
            11.3b shows that shear is dominant for all particle sizes, but
            settling is equally important for d(particle) > 100 mm. Also,  Subscript  Motion     Equation Reference
            as noted in Section 10.3.1.2, e.g., Figure 10.11, for ‘‘mixing’’  B  Brownian motion    11.4
            and reaffirmed for flocculation, shear is effective in causing  SH  Fluid shear           11.5
            collisions only for eddies that are about the same size as the  S  Settling             11.6
            particles (Casson and Lawler, 1990).
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