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184                                     6  Separation of Particles from a Gas

                                      64lLU 0  1:5     3
                                 DP ¼     2  a   1 þ 56a                ð6:102Þ
                                        d
                                         f
            where the pressure drop DP is in Pascal. It is thus directly proportional to thickness
                                                                         2
            of the filter L and inversely proportional to cross section area of the fiber d .
                                                                         f
              From the staggered array model, Yeh and Liu [38, 39] calculated the drag force
            over the fibers as
                                             4plU 0
                                        F D ¼                           ð6:103Þ
                                               Y
            and the corresponding pressure drop per unit thickness of the filter is


                                             16laU 0
                                         0
                                       DP ¼                             ð6:104Þ
                                              Yd 2
                                                f
              Then the total pressure drop over the entire array is determined as
                                               16LlaU 0
                                            0
                                   DP ¼ LDP ¼       2                   ð6:105Þ
                                                 Yd
                                                    f
              The corresponding pressure drop coefficient can then be determined by com-
            paring Eq. (6.105) with (6.100).

                                               4a
                                         C DP ¼                         ð6:106Þ
                                               Y
              With Y in the denominator, Yeh’s equation is complicated in form. In addition,
            as seen in Fig. 6.15, Yeh’s model gives greater pressure drops than Davies model.
              Figure 6.15 is produced for a filter with d f =10 µm, U ∞ = 0.2 m/s for
            α = 0.0–0.10 and L = 5, 10, 20 mm.
              First of all, the pressure drop increases with filter solidity; the relationship based
            on these equations is not linear, so the pressure drop begins to dramatically increase
            as solidity increases. Increasing the thickness of the filter also causes the pressure
            drop to increase, but this increase is linear as the factor for thickness is not raised to
            any exponent and acts as a scalar quantity in the relationship (thus, this would also
            be true for velocity). Both of these responses make intuitive sense, as logically one
            would expect that the addition of filter material (whether by increasing solidity or
            thickness) would increase the pressure drop.
              When comparing these two different models, it is clear that, for the same filter
            and operating conditions, Yeh’s equations predict a greater pressure drop. Yeh’s
            equations predict pressure drops about 1.5 times higher than Davies’s. When
            solidity is 1 (though, this may be outside of the equation’s domain), the result of
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