Page 182 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
P. 182

Grit Chambers                                                                                    137



                           TABLE CD7.1
                           Solution for Example 7.1—Shield’s Equation for Scour in Grit Chamber
                           v c                               g                    d          v c
                                                               2
                           (m=s)        b         f        (m=s )      SG        (m)        (m=s)
                           (a) Scour velocity for 0.2 mm quartz particle:
                                       0.06      0.03       9.81       2.65     0.0002      0.23
                           (b) Diameter of quartz particle scoured at 0.3 m=s(1 ft=s) and sensitivity to constants, b and f:
                           0.30        0.06      0.03       9.81       2.65     0.0004
                           0.30        0.08      0.023      9.81       2.65     0.0002
                           (c) Size of organic size matter scoured at SG ¼ 1.2 and 1.05:
                           0.30        0.06      0.03       9.81       1.2      0.003
                           0.30        0.06      0.03       9.81       1.05     0.012

                           Source: Londong, J., Water Sci. Technol., 21, 13, 1989.





              Example 7.1 Scour Velocity in Grit Chamber       cross-sectional area, it follows that A must be a linear function
              (Adapted from Camp, 1946)                        of Q if v H is held constant, that is,

              Problem Statement                                                    Q ¼ v H   A              (7:2)
                (a) Estimate the highest velocity in a grit chamber to
                   avoid scour of sand particles 0.2 mm is size.  where v H ¼ 0.3 m=s (1.0 ft=s)—a constant. This mathematical
                (b) Determine the sand size that will be started in  condition can be accomplished by several methods, described
                   incipient motion if the velocity is 0.3 m=s (1.0 ft=s).
                                                               in the following sections.
                (c) Determine the size of organic matter (assume
                   SG ¼ 1.2 and then 1.05) that will be scoured.
                (d) Look at any other variations that may be of interest.  7.2.2.1  Proportional Weir
                                                               For channels with vertical walls, the width, w, is constant, and
              Solution                                         therefore the depth must be a linear function of flow, Q.A
              The most expedient means to solve (a), (b), and (c) is by  proportional weir, shown in Figure 7.3, has this characteristic,
              means of a spreadsheet, that is, Table CD7.1, which is  that is, Q ¼ kd. The proportional weir may be dimensioned by
              based on the Shield’s equation.                  Equations 7.3 through 7.5. Terms are defined in Figure 7.3.
              Comments                                            To expand further, a proportional weir is a plate that
              The Shield’s equation is used to estimate design limits  fits across the channel (Figure 7.3). Below the weir, a free
              for channel velocity for a horizontal flow grit chamber.
              With respect to task (d), once set up, as in Table CD7.1,
              the algorithm can be used in a sensitivity analysis to
              assess the effect of errors, in choosing b and f and
              the effects of varying v c on particle sizes that may be
              scoured, etc.
                                                                                    C L



            7.2.2 HORIZONTAL VELOCITY CONTROL
            As noted in Section 7.2.1.2, the importance of maintaining a
                                                                                         x
            constant horizontal flow velocity of 0.3 m=s (1.0 ft=s) has long                             y  h
            been understood. The use of two or more parallel channels
            will accomplish this; a number of such examples are given in
            Metcalf and Eddy (1916). In other words, as flow increases                                  a
            above a certain ‘‘set-point,’’ the second grit chamber will                      b
            come into operation. Practice, however, has favored a single
            channel having some method for velocity control to maintain  FIGURE 7.3  Proportional weir—used with grit chambers to main-
            constant v H . Since flow, Q, is the product of v H and A, the  tain constant velocity.
   177   178   179   180   181   182   183   184   185   186   187