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COAGULATION AND FLOCCULATION 6-35

                   n       rotational speed, revolutions/s
                   D  i         impeller diameter, m
                                        3
                   r       density of liquid, kg/m
          The impeller constant of a specific impeller can be obtained from the manufacturer. For the radial-
          flow impeller of  Figure 6-18 , the impeller constant is 5.7, and for the axial-flow impeller it is 0.31.

            Example 6-7.   Design a cylindrical flash mixing basin by determining the basin volume, tank
          diameter, dimensions, required input power, impeller diameter from manufacturer’s data pro-
          vided below, and its rotational speed using the following parameters:
                                       3  3
                 Design flow rate     11.5     10   m  /d
                Rapid mix  t      5 s
                                    1
                Rapid mix  G      600 s
                Water temperature     5 	 C
                Place impeller at one-third the water depth
            From manufacturer’s data, the following impellers are available:
           Impeller type  Impeller diameters (m)  Power number (N p )
           Radial        0.3      0.4     0.6         5.7
           Axial         0.8      1.4     2.0         0.31

            Solution:
                                 3
                                           3
                                    3
                a.  Convert 11.5     10   m  /d to m  /s.
                                                 3
                                                    3

                                           .
                                        11 5 10 m /d             3
                                                         0133 m /s
                                                           .
                                          ( 86 400 s/d)
                                             ,
               b.  Using  Equation 6-13 , determine the volume of the rapid mix basin.
                                                     3
                                    V   Qt    (0133.  m /s )(5 s )    0665.  m 3

               c.  Using the radial impeller guidance from  Table 6-5 , assume  H / T     2.0, that is  H      2 T.
                 For a round mixing tank
                                                        2
                                                    ()
                                                     T
                                                          2
                                               V         ( T )
                                                     4
                 and
                                                      /
                                       ⎧ () (  .  3  1 3
                                         40 665 m ) ⎫ ⎪
                                   T   ⎨            ⎬     0751 or.  0 75 m
                                                                      m
                                                                  .
                                       ⎩ ⎪   2      ⎭
                 and
                                            H   2(0.75m)   1.5m
                 and because the impeller is at 1/3 water depth
                                          B   (0 333 )(1 5 m )    0 5 m
                                                     .
                                                              .
                                                .
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