Page 253 - Packed bed columns for absorption, desorption, rectification and direct heat transfer
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                                  Table 20. Values of the constants A, m and n in Eq. (146) taken from Ranrm [96]
                            Author              Packing               A              m     «
                            Van Krevelen [133]  Rings, coke and others  0.00595      0.67  0.33
                            Ziparis [132]       Rings §-20 mm         0.0021         0.75  O.S
                            Fujita and Hayakawa  Rings 5-35, Saddles 13-40        » 0.67   0.5
                            [134]               mm                    0.0251—1
                                                                           1 s J
                            Onda, Sada, Murase  Rings 6-10 mm         0.0107         0.9   0.5
                            [135]
                            Onda, Sada, Otubo [136]  Rings 6-10 mm    0.00625        0.5   0.5
                            Sherwood,           Rings 25-50 mm        0.00204        0.78  0.5
                            HollowEy[137]
                                                Rings 12,5 mm         0.00333        0.65  0.5
                                                Saddles 12.5-38       0.00285        0.72  0.5
                            Yoshida, Koyanagi [138]  Rings 15-25; Saddles 12-25   *   0.5  0.5
                                                mm


                            Hikita, Ono [139]   Fully wetted single element           0.545  O.S

                                                                           \  J
                            Ramm, Chagina [140]  Raschig Rings 25 and 50 mm  0.00216  0.77  0.5
                                                Pall Rings 50 mm      0.0036          0.77  0.5
                            Ramm, Chagina [140]  Raschig Rings 25 and 50 mm  0.00216  0.77  0.5
                                                Pall Rings 50 mm       0.0036         0.77  0.5




                                  The comparison of the constants given in Table 20 shows that usually
                          the power n at Set is equal to 0.5. This value is obtained theoretically in the
                          models of Higbie [1], Danckwerts [2] and Levich [3] and is experimentally
                           proved in the investigation of Sherwood and Holloway [137]. The value of the
                           power equal to 0.33 given by Van Krevelen [133] is for SCG in case of gas-side
                           controlled mass transfer.
                                  Equations with powers at the liquid superficial velocity, quite different
                           than those presented in Table 20, are proposed by Koch et al. [218] and by
                           Rixon [219]. They are as follows:


                               = 0.25(LJ  ,0.96                                             (147)
                             ia
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