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05_chap_wang.qxd  05/05/2004  3:46 pm  Page 212
                    212                                                    Lawrence K. Wang et al.

                    Table 4
                    Schmidt Numbers for Compounds in Water at 68°F and 1 atm
                    Solute a                Sc  b              Solute a                 Sc
                                              L                                           L
                    Oxygen                  558                Glycerol                 1400
                    Carbon dioxide          559                Pyrogallol               1440
                    Nitrogen Oxide          665                Hydroquinone             1300
                    Ammonia                 570                Urea                      946
                    Bromine                 840                Resorcinol               1260
                    Hydrogen                196                Urethane                 1090
                    Nitrogen                613                Lactose                  2340
                    Hydrogen chloride       381                Maltose                  2340
                    Hydrogen sulfide        712                Mannitol                  130
                    Sulfuric add            580                Raffinose                2720
                    Nitric acid             390                Sucrose                  2230
                    Acetylene               645                Sodium chloride           745
                    Acetic acid            1140                Sodium hydroxide          665
                    Methanol                785                Carbon dioxide c          445
                    Ethanol                1105                Phenol c                 1900
                    Propanol               1150                Chloroform c             1230
                    Butanol                1310                Acetic acid d             479
                    Allyl alcohol          1080                Ethylene dichloride d     301
                    Phenol                 1200
                       a Solvent is water except where indicated.
                       b Sc = µ /P D , where µ and P are the viscosity and density of the liquid, respectively, and D is the
                         L   L  L  L     L    L                                             L
                    diffusivity of the solute in the liquid.
                       c Solvent is ethanol.
                       d Solvent is benzene.
                       Source: ref. 13.

                    2.4.4. Packed Tower (Wet Scrubber) Operation and Maintenance
                       As previously mentioned, the pressure drop (head loss) through a packed tower (see
                    Fig. 1b) has a major impact on the economics of a tower. When in the design phase, the
                    most accurate pressure drop data for a given packing should be provided by the packing
                    supplier. However, for the purpose of a general example, the following is a relatively
                    accurate correlation:
                                         P = (     −8 )[  ( rL D L )  G ) 2
                                                          ′′
                                          a   g × 10  10     ](3 600,  area  D G              (21)
                                                     2
                    where P is the pressure drop (lb/ft -ft) and g and r are the packing constants from
                            a
                    Table 5 (4).
                       The total pressure drop through a packed tower (see Fig. 1b) wet scrubber is
                                                   P   = P Ht                                 (22)
                                                    total  a  column
                       The fan power requirement, F (in kWh/yr), is calculated as follows:
                                                 p
                                            F = 1.81 × 10 −4  (Q )(P  )(HRS)                  (23)
                                             P              e,a  total
                    where F is the fan power requirement (kWh/yr), Q  is the actual emission stream flow
                           P                                     e,a
                    rate (acfm), P  is the system pressure drop (in. H O), and HRS is the system operating
                                total                            2
                    hours per year (h/yr).
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