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Mixing                                                                                           273


                                                      Pressure differential, p (psi)
                                          0    50    100   150  200   250   300   350
                                     0.005
                                                                                     70
                                     0.004
                                                                                     60
                                              Nominal                                50
                                     0.003
                                    Q (m 3 /s)  range                                40  Q (gpm)
                                              operating
                                     0.002
                                                                                     30
                                                               Nozzle:
                                                               H-15, #15280, full cone  20
                                     0.001                     Spray angle 15°
                                                               d(orifice)=9.93 mm (0.391 in.)  10
                                                               Inlet connection: 1 in.
                                        0                                            0
                                          0       50      100     150     200      250
                                                            Head (m)

            FIGURE 10.22 Flow vs. head for nozzle. (Data from Spraying Systems Co., Wheaton, IL, Catalog 70, p. B28, 2010.)
              For a sharp edge orifice, C ¼ 0.611; also for any orifice,  Example 10.9 Design of Jet-Mixer System
            n ¼ 0.5, which conforms to value given in Catalog 70, p. B28
            for their nozzles. For a nozzle, the edge is not sharp and  Given
            differs for each model and so the discharge coefficient  Raw water is delivered to a WTP by a 1067 mm (42 in.)
            must be determined by a log–log plot such as shown. The  pipeline from Horsetooth Reservoir with water surface
                                                           ffiffiffiffiffi  elevation 61 m (200 ft) above the plant. Let T ¼ 208C for
            exponent, n, may be obtained from the same plot. The  2g
                                                         p
                                                                  working purposes.
            could be assimilated in a coefficient but is shown separate
            here (so that more variables can be discerned).       Required
                                                                  Design a jet-mixer system for coagulation.
            10.4.3.1.3  Design Algorithm
                                                                  Solution
            The design of a jet-mixing system is based first on knowing the
                                                                    1. General design
            relationship between flow and head, i.e., knowing the discharge
                                                                      Select Spraying Systems, nozzle H-15, #15280 (as
            coefficient in Equation 10.42 and=or a plot such as given in  in the plot shown in Figure 10.23)
            Figure 10.22 (or data from a catalog). The merit of an equation  The jets have a full cone spray with cone angle 158
            for the flow–head relationship is that it is amenable to use in a  Let n(nozzles) ¼ 24, intended to cover the cross-
            spreadsheet algorithm for design. The velocity of the jet may be  sectional area of the raw-water pipeline
            calculated from knowing the orifice diameter. The velocity  Let the jets be oriented radial direction outward
            head from the jet is dissipated as turbulence (with a portion,  from a center manifold
            not known, going to heat directly). The power required should  Let the coagulant (alum) be injected into the manifold
                                                                        flow just prior to the plane of the jet circle.
            be based on the head for the nozzle (not just the velocity head,
                                                                    2. Calculations
            since there is a loss of head through the nozzle). The wire-to-
                                                                      Set up a spreadsheet such as developed for the
            water power, i.e., the power required by the pump motor, may
                                                                      problem as Table CD10.12. The spreadsheet
            be calculated knowing the efficiency of the pump (in its oper-
                                                                      develops an algorithm to calculate for increasing
            ating range) and the motor efficiency. The cost of operation  manifold pressure: jet flow, jet velocity, assumed
            may be obtained from the local cost of energy per kilowatt-hour  pipe flow, jet flow as a fraction of raw-water flow,
            (kW-h). For initial estimates a pump efficiency of 0.7 and a  the power dissipated by the jet, the distance, Dz for
            motor efficiency of 0.7 may be used.                       the intersection of the jet trajectory with the pipe
              Example 10.9 enumerates a design algorithm for a jet-mixer  wall, the mixing time, the hypothetical mixing vol-
            system. The spreadsheet, Table CD10.12, shows for increasing  ume, G, Gu, pump power imparted to water,
            manifold pressure: the jet flow, jet velocity, assumed pipe flow,  energy use per month (based on assumed wire-
                                                                      to-water efficiency), monthly cost (based on an
            jet flow as a fraction of pipe flow, the power dissipated by the
                                                                      assumed cost of electric energy), and power dissi-
            jet, the distance, Dz for the intersection of the jet trajectory with
                                                                      pated per unit of flow (energy consumed per unit
            the pipe wall, the mixing time, the hypothetical mixing vol-
                                                                      of flow is about twice that calculated in Table
            ume, G, Gu, pump power imparted to water, energy use per
                                                                      CD10.12). Table CD10.12b shows advective tra-
            month (based on assumed wire-to-water efficiency, monthly  jectories for two jet flows. Figure CD10.23 is a
            cost (based on an assumed cost of electric energy), and power  linked plot, from trajectories restated in Table
            dissipated per unit of flow (energy consumed per unit of flow is  CD10.12f, showing how the trajectory is modified
            about twice that calculated in Table CD10.12).            by jet velocity.
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