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                    298                                                    Lawrence K. Wang et al.

                       Q            Actual emission stream flow rate (acfm)
                        e,a
                       Q            Actual flow rate of dry air (acfm)
                        e,ad
                       Q            Saturated emission stream flow rate (acfm)
                        e,s
                                                           3
                       Q            Volume of water added (ft /min)
                        w
                       r            Empirical packing constants (dimensionless)
                                                            3
                       R            Gas constant (0.7302 atm-ft /lb-mol°R)
                       RE           Removal efficiency (%)
                       RE           reported removal efficiency (%)
                         reported
                       s            Empirical packing constant (dimensionless)
                       Sc           Schmidt number for gas stream
                         G
                       Sc           Schmidt number for liquid stream
                         L
                       S            Specific gravity of fluid
                        g
                       SG           Specific gravity of the plastic or other material used to produce the media
                         media
                       SG           Specific gravity of water (=1)
                         water
                       T            Temperature of gas (°R)
                       TAC          Total annual cost ($)
                       TCC          Total capital cost ($)
                       T            Temperature of the emission stream at inlet air (°F)
                        e
                       T            Temperature of the saturation emission stream (°F)
                        e,s
                       UEC          Unit electricity cost ($/kWh)
                       USC          Unit cost of the solvent ($/gal)
                                                       3
                       V            Volume of packing (ft )
                        packing
                       VSC          Venturi scrubber cost ($)
                                                       3
                       W            Weight of media (lb/ft )
                        media
                       WR           Water consumption (gal/yr)
                                                           3
                       W            Weight of water (62.4 lb/ft )
                        water
                       Y            Empirical packing constant (dimensionless)
                       µ L          Viscosity of scrubbing liquor (cP [1 when using water ])
                       µ L''        Liquid viscosity (lb/ft-h)
                       µ            Micrometer (1×10 m)
                                                    −3
                        m
                    REFERENCES
                     1. R. H. Perry, and, C. H. Chilton (eds.), Chemical Engineer’s Handbook, 6th ed., McGraw-
                        Hill, New York, 1980.
                     2. R. E. Treybal, Mass Transfer Operations, 3rd ed., McGraw-Hill, New York, 1980.
                     3. US EPA, Wet Scrubber System Study, Vol. 1: Scrubber Handbook, EPA-R2-72-118a (NTIS
                        PB 213016), US Environmental Protection Agency, Washington, DC, 1972.
                     4. US EPA,  Organic Chemical Manufacturing, Vol. 5: Adsorption, Condensation and
                        Absorption Devices, EPA-450/3-80-027 (NTIS PB 81-220543), US Environmental
                        Protection Agency, Research Triangle Park, NC, 1980.
                     5. W. M. Vatavuk, and R. B. Neveril, Chem. Eng. NY, Oct. 4 (1962).
                     6. A. Kohl, and F. Riesenfield Gas Purification, 2nd ed., Gulf Publishing, Houston, TX, 1974.
                     7. R. S. Hall, W. M. Vatavuk, and J. Matley, Chem. Eng. NY, Nov. 21 (1988).
                     8. Michael Sink of Pacific Environmental Services, Inc. to Koch Engineering, Inc. and
                        Glitsch, Inc., Costs of tower packings, Telecommunications, Research Triangle Park, NC,
                        Jan., 1990.
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