Page 143 - Packed bed columns for absorption, desorption, rectification and direct heat transfer
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                           A,=H la el-H la.                                                 (73)


                           2.1,2.5.11. Comparison of the methods for determination of the effective surface
                           area
                                  The comparison of the methods for determination of the effective
                           surface area of packed bed columns shows that the best of them is the method of
                           Danckwerts [39], and especially the variant with absorption of CO2 in solutions
                           of NaOH (or KOH). Good results are also obtained using the method of
                           Schulman [31]. It was found [40] that the results obtained using both these
                           methods are practically the same. The comparison is made at comparatively low
                           liquid superficial velocities when the effective area of the jets and drops in the
                           packing void fraction can be neglected. This is important mentioning because an
                           investigation with modern packings carried out at very high liquid superficial
                                              2  2
                           velocity, up to 200 (m /m h) [5] shows, that the effective surface of the packing
                           is quite greater, up to two times, than its specific surface. It is clear that no
                           method, based on the wetted or effective surface of the packing elements, can
                           be useful for predicting the effective area of the packing at such conditions.
                           That is, the only method useful for all hydrodynamic regimes in packed bed
                           columns is that of Danckwerts [39]. Nevertheless, at low liquid superficial
                           velocities the other methods, like those of van Krevelen et al. [27], and Shulman
                           et al. [31], can be also used.
                                  The methods for determination of the wetted surface area do not have
                           now any practical importance.
                                  New information about the problem connected with prediction of the
                           effective surface by physical absorption, using the method of Danckwerts, is
                           given by Last and Stichlmaier [102,103]. Their investigations are carried out
                           with one and the same packing and liquid superficial velocity for absorption
                           accompanied by two different chemical processes. The first of them is
                           absorption of CO2 from air in 1 N KOH solution (the Danckwerts method), and
                           the second - absorption of CO2 in water solution of methyldiethanolamin
                           (MDEA). The authors [102,103] show that the effective surface area determined
                           by the first reaction is up to 5 times greater than in case of physical absorption.
                           In case of CO2 absorption in MDEA, the difference is 50%. In their
                           investigations Last and Stichlmaier [102-103] used own results [105, 109] for
                           determination of mass transfer parameters in chemical absorption. The big
                           difference in the effective surface for different processes is explained with
                           presence of stagnant zones of absorbent on the packing surface. In case of
                           nonequilibrium reaction (Danckwerts method), the liquid in these zones is
                           saturated for longer time with the absorbed gas than in case of physical
                           absorption. This results in determination of higher effective surface area. The
                           same reason explains also the difference in the second chemical reactions.
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