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6-26   WATER AND WASTEWATER ENGINEERING

                            circuiting because of uneven inlet or outlet conditions, and local turbulence or dead spots in the
                            reactor corners. The mean detention time in real tanks is generally less than the theoretical deten-
                            tion time calculated from  Equation 6-13 .

                              Selection of  G  and  Gt  Values
                             Both  G  and the product of the velocity gradient and time ( Gt ), serve as criteria for the design of
                            mixing systems. The selection of  G  and  Gt  values for coagulation is dependent on the mixing
                            device, the chemicals selected, and the anticipated reactions. As noted previously, coagulation
                            occurs predominately by two mechanisms: adsorption of the soluble hydrolysis species on the
                            colloid and destabilization or sweep coagulation where the colloid is trapped in the hydroxide
                            precipitate. Jar test data may be used to identify whether adsorption/destabilization or sweep
                            coagulation is predominant using the following procedure:
                                  •  Determine the optimum pH and dose from plots of settled turbidity (see, for example,
                                   Figure 6-11 ).

                                 •  Plot the optimum pH and dose on  Figure 6-9 .
                                 •  Determine which is the predominant mechanism from the plotted position.
                                                                       1
                                   G  values in the range of 3,000 to 5,000 s    and detention times on the order of 0.5 s are
                            recommended for adsorption/destabilization reactions. For sweep coagulation, detention times of
                                                                            1
                            1 to 10 s and  G  values in the range of 600 to 1,000 s    are recommended (Amirtharajah, 1978).

                             6-7   MIXING PRACTICE
                              Although there are some instances of overlap, mixing equipment may be divided into two broad
                            categories: equipment that is applicable to dispersion of the coagulant into the raw water and that
                            used to flocculate the coagulated water. Dispersion of the coagulant into water is called  flash
                            mixing or  rapid  mixing.

                                Flash Mixing Design Criteria
                             This equipment is designed to produce a high  G.  The order of preference in selection of equip-
                            ment type is based on effectiveness, reliability, maintenance requirements, and cost. Common
                            alternatives for mixing when the mechanism of coagulation is adsorption/destabilization are:

                                  1.  Diffusion mixing by pressured water jets.
                                 2.  In-line mechanical mixing.
                                 3.  In-line static mixing.

                            Common alternatives for mixing when the mechanism of coagulation is sweep coagulation are:
                                  1.  Mechanical mixing in stirred tanks.
                                 2.  Diffusion by pipe grid.
                                 3.  Hydraulic mixing.
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