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Grit Chambers                                                                                    157



            TABLE CD7.14
            Airflow and Power Calculations for Aerated Grit Chamber
               1 Coefficients               2 Constants
                 Diffuser Type     Constant  Value   Units
            Coeff. Coarse  Fine        R ¼  8.314510  J K mol  1
                                                       1
                                           0.028964  kg=mol
                   0.07  0.63     MW(air) ¼
             a ¼
                                           1.395
                   0.76  0.52          k ¼
             b ¼
                   1.33  0.62
             c ¼
                             3 Air Flow Calculations                          4 Compressor Power Required
            d(diff)  Q(air, co)  Q(air, f )  V(Gr Ch)  Q(air)  Elev.  p(atm)  T  r(air)  r(air)  p 2    P
                                          3
                              3
                     3
                                                                                  3
                                                 3
                                                                                          3
            (m)    (m =m=h)  (m =m=h)   (m )   (m =s)    (m)      (Pa)  8C   (mol=m )  (kg=m )  (Pa)   (kW)  (hp)
            0.90    >1000     1.409     375      0.1      0     101325  20    41.57    1.204  303975    21   27.5
            1.00    34.357    1.332     375      0.1      0     101325  20    41.57    1.204  303975    19   25.9
            1.50    3.645     1.113     375      0.1      0     101325  20    41.57    1.204  303975    16   21.7
            2.00    1.987     1.006     375      0.1      0     101325  20    41.57    1.204  303975    15   19.6
            2.50    1.425     0.939     375      0.1      0     101325  20    41.57    1.204  303975    14   18.3
            3.00    1.142     0.893     375      0.1      0     101325  20    41.57    1.204  303975    13   17.4
            5 Notes on columns and equations
                                3
                    Dimensions are m air flow (at normal temperature and pressure) per hour  Assumed  Diffuser p þ Dp(losses)
                                 3
                             per m of grit chamber volume
                                  c
                    Q(air) ¼ [a þ b ln(d)] (from Londong, 1989)
                                               Q(air) ¼ Q(air, fine)   V(Gr Ch)
            d(diff) ¼ depth of diffuser
                                      V(Gr Ch) ¼ w   D   L      Use barometric pressure or default value adjusted for elevation,
                    Q(air, co) ¼ air flow for coarse bubble diffuser  Assumed  that is, p(atm) ¼ 101,325 * 10  0.00005456*Z
                              Q(air, f) ¼ air flow through fine bubble diffuser  r(air) ¼ p(atm)=RT
                              3
                                                                                                   3
            Alternatively, Q(air) ¼ 3–8ft =min=ft length (ASCE, 1977)                  r(air) ¼ p(mol=m ) * MW(air)=1000
                                      3
                         ¼ 0.0046–0.0124 m =s=m length of tank
            Power required by compressor is for an adiabatic compression and is calculated by relations in Table 7.13

            compressor for an adiabatic compression for different depths  7.1 Rectangular Grit Chamber with Proportional Weir
            of diffuser submergence. The spreadsheet (on a CD) also has  Control
            the same table in U.S. Customary units.                Given
              The pressure, p 2 , on the discharge of the compressor was                     3
                                                                   Assume flows: Q(avg) ¼ 0.22 m =s (5 mgd), Q(min) ¼
            assumed as p 2 ¼ 3   p(atm), which was an arbitrary assumption  0.30   Q(avg), and Q(max) ¼ 3   Q(avg).
            for the purpose of illustrating the spreadsheet functioning. The
                                                                   Required
            value of p 2 should be calculated by Equation 7.26, which
                                                                   Design a rectangular grit chamber with a proportional
            requires another linked spreadsheet and involves utilizing
                                                                   weir as control.
                                                               7.2 Rectangular Grit Chamber with Parshall Flume
            submergence depth, for example, Dp(submergence) ¼
            r(water)   g   z(submergence), determining pipe sizes, and cal-
                                                                   Control
            culations such as pressure losses due to pipe friction, for
            example, by the Darcy–Weisbach equation, and minor losses  Given
                                                                                       3
            for valves, a flow meter, etc.                          Flows: Q(avg) ¼ 0.22 m =s (5 mgd), Q(min) ¼ 0.30
                                                                   Q(avg), and Q(max) ¼ 3   Q(avg).
                                                                   Required
            PROBLEMS                                               Design a rectangular grit chamber with a Parshall flume
                                                                   as control.
            Given Conditions
                                          3                    7.3 Parabolic Grit Chamber with Parshall Flume Control
            For all problems, let Q(avg) ¼ 0.22 m =s (5 mgd), Q(min) ¼
            0.30   Q(avg) and Q(max) ¼ 3   Q(avg), unless otherwise spe-  Given=Required
            cified. Use a spreadsheet for each problem unless advised  Design a parabolic section grit chamber with a Parshall
            otherwise.                                             flume as control.
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