Page 324 - Fundamentals of Water Treatment Unit Processes : Physical, Chemical, and Biological
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Mixing                                                                                           279




                                          G  (s  1 )  7968  2911  1333  704  411  257  1333  1333  1333  1333  471  1333  2449  3771


                                            (kW=m 3 )  83.30  11.12                  18.66
                                          P=V         2.33  0.65  0.22  0.09  2.33  2.33  2.33  2.33  0.29  2.33  7.87



                                          V(mixer)  (m 3 )  0.321  0.766  1.487  2.570  4.081  6.092  0.744  1.115  1.487  2.231  1.487  1.487  1.487  1.487  A   L  ¼ V  (2001)


                                                                                          Kenics  Q   (rg)   h L
                                            (W)     8513  3468  1673  903  529  1734  2601  3468  5202  434  3468  ¼
                                          P      26761                             11705  27746  f(L=D)(v 2 =2g)  of  units  P



                                          h L  (m)  3.922  1.248  0.508  0.245  0.132  0.078  0.254  0.381  0.508  0.762  0.127  0.508  1.144  2.033  ¼ h L  on  based


                                          L(mixer)  (m)  1.96  2.623  3.26  3.91  4.57  5.22  1.63  2.45  3.26  4.89  3.26  3.26  3.26  3.26  (2001)  Calculated



                                          Elements  (#)  4  4  4  4  4  4  2  3  4  6  4  4  4  4  al.  et  Trial




                                            f    1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  1.0  Amirtharajah



                                            R    1476889  1107667  886134  738445  632953  553834  886134  886134  886134  886134  443067  886134  1329200  1772267  rvd=m  ¼
                                                                                       R

                                          v(pipe)  (m=s)  4.2  2.4  1.5  1.1  0.8  0.6  1.5  1.5  1.5  1.5  0.8  1.5  2.3  3.1  Q=A  ¼

                                                                                       v

                                  Mixer  d(pipe)  (m)  0.457  0.610  0.762  0.914  1.067  1.219  0.762  0.762  0.762  0.762  0.762  0.762  0.762  0.762

                                  Static    (in.)  18  24  30  36  42  48  30  30  30  30  30  30  30  30  Trial


                                  for       (m 3 =s)  0.696  0.696  0.696  0.696  0.696  0.696  0.696  0.696  0.696  0.696  0.348  0.696  1.044  1.392
                                  Calculations  Q  (mgd)  20  20  20  20  20  20  20  20  20  20  10  20  30  40  Given





                                  G
                                  P,      r(water)  (kg=m 3 )  selection  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  999.7  Calculated
                                  Headloss,    and              elements    variation
                               CD10.14  of  m=s 2  m(water)  s=m 2 )  (N  d(pipe)  of  0.001312  0.001312  0.001312  0.001312  0.001312  0.001312  #  of  0.001312  0.001312  0.001312  0.001312  flow  of  0.001312  0.001312  0.001312  0.001312  Calculated




                               TABLE  Example  9.80665  ¼ g  T  (8C)  Effect  (a)  20  20  20  20  20  20  Effect  (b)  20  20  20  20  Effect  (c)  20  20  20  20  Given
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