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Mixing                                                                                           263



                                                               where
                                                                  n(impeller) is the rotational velocity of impeller (rev=s)
                                                                  t 5R   time for five circulations through impeller (s)
                                                                    ¼ 5   u(impeller)
                                                                  K(0.99 blend) is the mixing constant for 0.99 fraction
                                                                    blend valid for turbulent zone (dimensionless)

                                                                  The ‘‘blend number,’’ i.e., ‘‘n(impeller)   t 5R ,’’ is designated
                                                               here as K(0.99 blend) and is constant in the turbulent range, i.e.,
                                                               high R. The blend numbers for four systems are given in Table
                                                               10.6 and illustrate range in values, e.g., 36   K(0.99 blend,
                                                               turbines)   60; and 120   K(0.99 blend, propellers)   550. The
                                                               utility of the blend number is that from it the rotational velocity
                                                               of the impeller, n(impeller), may be estimated.
                                                                  To illustrate how the blend number may be used,
                                                               assume the system is a turbine in a baffled tank, in which
                                                               K(0.99 blend) as in Table 10.6, and assume that u(raw
                                                               water) ¼ 10 s.
                                                                  First, from Equation 10.35,
                                                                          n(impeller)   t 5R ¼ K(0:99 blend)


                                                               and since we let

                                                                         t 5R ¼ 5   u(impeller) ¼ u(raw water),
              (a)
                                                               then,

                                                                      n(impeller)   u(raw water) ¼ K(0:99 blend)


                                                               Next, substitute numerical values, i.e., u(raw water) ¼ 10 s,
                                                               and from Table 10.6, for a turbine in a baffled, tank, K(0.99
                                                               blend) ¼ 36, to give

                                                                              n(impeller)   (10s) ¼ 36

                                                               Thus, n(impeller) ¼ 3.6 rev=s.


              (b)
                                                               TABLE 10.6
            FIGURE 10.17 Two kinds of impeller mixer systems. (Courtesy of
            City of Fort Collins Utilities, Fort Collins, CO, 2010). (a) Back-mix  Values of ‘‘Blend Number,’’ K(0.99 Blend)
            reactor. (b) In-line mixer.                        Impeller Type  Conditions  D=T b  H=T b  R c  K(0.99 Blend)
                                                               Propeller             1=6  1.0   20,000    550
            where                                              Propeller             1=3  1.0   20,000    120
                                                         3
              Q(neat alum) is the flow of neat alum into reactor (m =s)  Turbine a    1=3  1.0   4,000     60
              C(neat alum) is the concentration of neat alum solution as  Turbine  Baffled  1=3  1.0   2,000  36
                                                        3
                provided by manufacturer (647 kg neat alum=m neat
                alum solution)                                 Source: Adapted from McCabe, W.L. et al., Unit Operations of Chemical
                                                                      Engineering, 5th edn., McGraw-Hill, New York, p. 259, 1993.
                                                               a  A turbine is a radial-flow impeller.
            10.4.1.2.1  Blend Number
                                                               b  D, diameter of impeller; T, diameter of tank; H, depth of water; R,
            The product ‘‘n(impeller)   t 5R ’’ is a constant for a given sys-
                                                                 Reynolds number.
            tem (McCabe et al., 1993, p. 258), i.e.,           c  Threshold value of Reynolds number at which K(0.99 blend) becomes
                                                                 constant.
                    n(impeller)   t 5R ¼ K(0:99 blend)  (10:35)
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