1.
85 WATER AND WASTEWATER TREATMENT ENGINEERING
                              HOMEWORK 4
Question 1 (5 points)
   A suspension of three sizes of spherical particles is to be filtered at a rate of 15 m/hr through
   a 60-cm rapid sand filter. The bed sand has a diameter of 0.5 mm and a porosity of 0.4.
   Particle counting indicates that there are 5, 25, and 125 mg/L each of 0.1, 1.0, and 10.0-
   micron diameter particles, respectively. The particles have a density of 1.05 g/cm3. The
   water temperature is 25C.
       a. 	 Assuming discrete particle settling, determine the single collector efficiency, , for
            each particle size using the theoretical model of Yao et al. (1971) as given in the
            notes for Lecture 7. (2 points)
       b. 	 If the attachment efficiency, , is 0.2, what is the concentration of each particle after
            the water passes through the filter bed? (2 points)
       c. 	 If the attachment efficiency, , is 1.0, what is the concentration of each particle after
            the water passes through the filter bed? (1 point)
Question 2 (5 points)
   Design a sedimentation treatment system for a raw water with the following characteristics:
       Maximum daily flow = 4 m3/s
       Average daily flow = 3 m3/s
       Coagulant = alum
       Settling velocity for floc = 3.2 m/hr
       Your design should be for a horizontal-flow rectangular basin with a chain and scraper
       sludge removal system. You can assume a dynamic viscosity for water of 0.00131
       kg/m-s and a density of 999.7 kg/m3. You should specify the number of sedimentation
       basins, the basin dimensions, and the basin overflow rate and hydraulic residence time.
       Sludge scrapers come in a standard 6-meter length, so your basin width should be in
       increments of 6 meters. Design guidelines for horizontal-flow rectangular tanks are
       excerpted below from MWH (2005):
                          Parameter                              Units                      Value
        Minimum number of tanks*                                Unitless                       2
        Water depth                                             Meters                      3 to 5
        Minimum length-to-depth ratio                           Unitless                     15:1
        Width-to-depth ratio                                    Unitless                  3:1 to 6:1
        Minimum length-to-width ratio                           Unitless                  4:1 to 5:1
        Overflow rate                                            m/hr                    1.25 to 2.5
        Horizontal mean-flow velocity = Vf                       m/min                    0.3 to 1.1
        Detention time                                            hr                       1.5 to 4
        Outlet weir loading rate                                m3/m-hr                    9 to 13
       * 	Number of tanks should be sufficient to allow one tank to be taken off-line for maintenance without
          causing overloading of remaining tank(s).