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312                                                      Chapters

           Example 6.5  Sizing a Rotary-Drum Filter____________________


           A  rotary-drum  filter  filters  20 m3/h (706 ft3/h)  of  a  calcium  carbonate  slurry  at
            20 °C (68 °F).  The  pressure  drop  across the  cake  is 0.658 bar  (9.541 psi). If  the
            slurry  contains 0.15  mass  fraction  of  calcium carbonate,  and  the  filter  cake con-
           tains 0.40 mass fraction  of water,  estimate the  surface  area of the rotary-drum fil-
           ter.

           Data
                                         3
                                                  3
           water density        998.3 kg/m  (62.3 Ib/ft )
           water viscosity (20 °C)  0.001  Pa-s (1 cp)
                                                  3
                                         3
            CaCO 3 density      2709 kg/m  (169 Ib/ft )
                From  Equation  6.18.3,  y  =  0.85, and from  Equation  6.18.7  the  average
                                    u
           density of the slurry,
                                               3
                                                         3
            P! = 0.85 (998.3) + 0.15 (2709) = 1255 kg/m  (78.35 Ib/ft )
                Equation 6.18.4 gives y C2 = 0.60. The formation rate of wet cake, me, can
           now be calculated from Equation 6.18.2.  Thus,

                0.15  1255  kg  20m 3
                                                       4
                                            3
           me = ——   —————    ——   = 6.275xl0  kg/h (1.3xl0  Ib/h)
               0.60    1  m 3  1 h
                The volumetric flow rate of the filtrate, V 2, obtained from Equation 6.18.1, is

                yi,i Pi Vj  -  y c,i me
           V,  =  ———————————

                      P2.1
                     0.85  1255  kg  20m 3
                                                             4
           YuPiV,   =——   ————    ——— =2.134x10* kg/h (4.71xl0 lb/h)
                       1    1  m 3  1  h
                                          3
                                                       3
           y c,i me = 0.40 (6275 kg/h) = 2.510xl0  kg/h (5.535xl0  Ib/h)
               21340-2510
                                  3
           V 2 = ———————   =18.86 m /h (666 ftVh)
                   998.3

                Table 6.17  does  not  contain  oc for  calcium  carbonate.  According  to  Walas
                                          0
            [6], the specific  cake resistance for filtering  CaCO 3, given by Equation 6.18.9, is



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