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03_chap_wang.qxd  05/05/2004  12:48 pm  Page 118
                    118                                                    José Renato Coury et al.

                    Table 6
                    Results from the Calculation of the Particle Size Distribution in the Cyclone Exit.
                    Range (µm)  D (µm)     η (20 m/s)    η x (20 m/s)    m (kg/s)     x (in mass)
                                  i         i             i i             oi           oi
                       0–1        0.5       0.00226       0.0000226     3.6158E-05      0.138877
                       1–2        1.5       0.07690       0.0015380     6.6906E-05      0.256976
                       2–4         3        0.44728       0.0178910     8.0123E-05      0.307739
                       4–6         5        0.81212       0.0487270     4.0853E-05      0.156911
                       6–8         7        0.92874       0.0742990     2.0661E-05      0.079354
                       8–10        9        0.96745       0.0967446     1.1798E-05      0.045312
                      10–20       15        0.99374       0.1291862     2.9493E-06      0.011328
                      20–30       25        0.99882       0.1498233     6.4035E-07      0.002459
                      30–40       35        0.99961       0.1199531     1.7004E-07      0.000653
                      40–50       45        0.99983       0.0999828     6.2154E-08      0.000239
                      50–60       55        0.99991       0.0699938     2.2529E-08      8.65E-05
                      60–70       65        0.99995       0.0499974     9.3040E-09      3.57E-05
                      70–80       75        0.99997       0.0399987     4.6551E-09      1.79E-05
                      80–90       85        0.99998       0.0199996     1.5439E-09      5.93E-06
                      90–100      95        0.99998       0.0099999     5.3597E-10      2.06E-06
                                                         Σ η x = 0.93  Σ m = 2.604E-4   Σ x = 1.0
                                                            i i           oi              oi




                       From Example 1, the pressure drop in cyclone operating with a particle-free gas at 20 m/s
                       was estimated using
                                                  ∆P at  c in 0  =  1510 Pa
                                                        =
                       Therefore, Eq. (35) gives

                                               ∆P
                                                  at  c in   . 0 013 8 (  .7)  . 05
                                                       =  1 −
                                               1510 Pa
                                                   ∆P at  c in  =  1452 Pa


                    3. COSTS OF CYCLONE AND AUXILIARY EQUIPMENT*
                    3.1. Cyclone Purchase Cost
                       Cyclones are used upstream (60) of particulate control devices (e.g., fabric filters,
                    ESPs) to remove larger particles entrained in a gas stream. Equation (44) yields the cost
                    of a carbon steel cyclone with support stand, fan, and motor, and a hopper or drum to
                    collect the dust:
                                                               0.9031
                                                  P cyc  =  6250A cyc                         (44)




                       *This subject is also presented in the chapter “Technical, Energy and Cost Evaluation of Air Pollution
                    Control Technologies”, by L. K. Wang et al. in Volume 2 of the Handbook of Environmental Engineering
                    series. The examples given here were taken from that chapter.
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