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ACTIVATED CARBON PROCESSES              14.37


         to  1,700  lb/ft 2 per  day  (7,125  to  8,300  kg/m 2 per  day).  These  numbers  are  based  on  the
         cross-sectional area perpendicular to the flow of combustion air. In an infrared furnace, car-
        bon flow depends  on the width of the conveyor belt and residence time.


         Regeneration  By-products
         Activated carbon must be regenerated in a way  that does not pollute the environment. For
        this reason, scrubbers and afterburners are used to minimize particulate and gaseous emis-
         sions,  respectively.  The  afterburner  oxidizes  organic  compounds,  and  the  scrubber  re-
        moves particulate  matter  and  any  soluble chemical  species  from  the  gas  stream.  Off-gas
        control  is  important in controlling dioxins  and  furans  produced  during regeneration.  For
        these reasons, local air quality regulations should be reviewed early in the design process.
        A  supplementary  dust  collector  is  used  only  where  it  is  necessary  to  collect  particulate
        matter not normally removed  by  scrubbers.


        Transporting  Carbon from  the Quench Tank
        Eductors  typically transport carbon away  from  the  quench tank.  The  quench  tank is nor-
        mally a  small  tank that receives  hot  regenerated  carbon from  the  furnace,  and  the  water
        level must be controlled to prevent hot carbon from being exposed to air. When a method
        other than  an  eductor  is used  to  transport  carbon,  the  volume  of makeup  water  must  be
        greatly  increased.  The  increased  volume  of  makeup  water  causes  turbulence  that  keeps
        carbon in suspension and increases carbon losses.  With an eductor,  most of the transport
        and dilution water  is  supplied by the  water treatment  system.



         BIBLIOGRAPHY

        Adsorption  of Pesticides  by Powdered Activated  Carbon. Denver, Colo.:  AWWA Research Founda-
         tion, American Water Works Association, 1994.
        Clark,  R. M.,  and B. W. Lykins, Jr. Granular Activated  Carbon Design,  Operation and  Cost. Boca
         Raton, Fla.: Lewis, undated.
         Control of Organic Compounds with Powdered Activated  Carbon. Denver, Colo.:  AWWA Research
         Foundation,  American Water Works Association,  1991.
         Crittenden, J. C.,  D.  W. Hand, H. Ariham, and B. W.  Lykins, Jr.  "Design Considerations for GAC
         Treatment of Organic Chemicals." Journal AWWA 79(1):74,  1987.
         Culp, R. L., and R. M. Clark.  "Granular Activated Carbon Installations." Journal AWWA 75(8):398,
         1983.
         "Design and Use of Granular Activated Carbon: Practical Aspects." Proceedings  Technology Trans-
         fer Conference. May 9 and 10,  1989. Denver, Colo.:  American Water Works Association, 1989.
         The Effect of Metals on Thermal Regeneration of Granular Activated  Carbon. Denver, Colo.: AWWA
         Research Foundation, American Water Works Association, 1994.
         GAC Filter Adsorbers.  Denver, Colo.:  AWWA Research Foundation, American Water Works As-
         sociation,  1987.
         Graese, S. L., V. L. Snoeyink, and R. G. Lee. "Granular Activated Carbon Filter-Adsorber Systems."
         Journal AWWA 79(12):64,  1987.
         The Hazardous  Potential  of Activated  Carbons  Used in  Water  Treatment.  Denver, Colo.:  AWWA
         Research Foundation, American Water Works Association, 1994.
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