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Adsorption                                                                                       507


                                                               . Morris, J. C. and Weber, W. J. Jr., Preliminary Appraisal of
                       Sieve Series     Sieve Opening
                                                                  Advanced Waste Treatment Processes, Technical Report W62-
                     Tyler    U.S.    (mm)      (in.)             24, September, 1962.
                                                               . Morris, J. C. and Weber, W. J. Jr., Adsorption of Bio-
                       4       3.5    5.660    0.223
                                                                  chemically Resistant Materials from Solution 1, AWTR-9, May,
                               4      4.760    0.187
                                                                  1964.
                               5      4.000    0.157           . Morris, J. C. and Weber, W. J. Jr., Adsorption of Biochemi-
                       6       6      3.360    0.132              cally Resistant Materials from Solution 2, AWTR-16, March,
                               7      2.830    0.111              1966.
                       8       8      2.380    0.0937          . Williamson, J. N., Heit, A. H., and Calmon, C., Evaluation of
                               10     2.000    0.0787             Various Adsorbents and Coagulants for Wastewater Renovation,
                      10       12     1.680    0.0661             AWTR-12, June, 1964.
                      12       14     1.410    0.0555          [Topics of other reports in the series included: AWTR-3 wet
                                                                    oxidation and incineration; AWTR-4 freezing; AWTR-5
                      14       16     1.190    0.0469
                                                                    foaming; AWTR-6 distillation costs; AWTR-7 distillation;
                               18     1.000    0.0394
                                                                    AWTR-8 ultimate disposal; AWTR-13 electrochemical
                      20       20     0.840    0.0331
                                                                    treatment; AWTR-17 market projections; AWTR-18 electro-
                      24       25     0.710    0.0280               dialysis.]
                               30     0.590    0.0232          Baker, M. N., The Quest for Pure Water, American Water Works
                      32       35     0.500    0.0197               Association, New York, 1948.
                      35       40     0.420    0.0165          Brooks, D. R., Personal communication, Calgon Activated Carbon
                      42       45     0.350    0.0138               Co., Pittsburgh, PA, 2003.
                      48       50     0.297    0.0117          Brunauer, S., Emmett, P. H., and Teller, E., Journal of the American
                      60       60     0.250    0.010                Chemical Society, 60, 309, 1938.
                                                               Calgon Carbon Corporation, Contaminated groundwater cleaned by
                      65       70     0.212    0.008
                                                                    granular carbon system, http:==www.calgoncarbon.com=arti-
                      80       80     0.180    0.007
                                                                    cles, February 17, 2003a.
                     100      100     0.150    0.006
                                                               Calgon, Filtrasorbt 300 & 400, Product Bulletin, PB-1042-08=98,
                                                                    Calgon Carbon Corporation, Pittsburgh, PA, http:==www.cal-
                                                                    goncarbon.com, 2003b.
            Wave front: The portion of the concentration profile, i.e.,  Cannon, F. S., Snoeyink, V. L., Lee, R. G., Dagois, G., and
                   C(Z) t curve, which is the reaction zone of the reactor.  DeWolfe, J. R., Effect of calcium in field-spent GAC’s
                   Same as ‘‘mass-transfer zone.’’                  on pore development during regeneration, Journal of the
                                                                    American Water Works Association, 85(3):76–89, March,
                                                                    1993.
            REFERENCES                                         Champlin, T. L. and Hendricks, D. W., Treatment train modeling
                                                                    for aqueous contaminants, Volume II, Matrix of contamin-
            Abdelrasool, F., Kinetics of adsorption, PhD thesis, Department of  ants and treatment technologies, Environmental Engineering
                Civil Engineering, Colorado State University, Fort Collins,  Technical Report 53-2415-93-2, Department of Civil Engin-
                CO, 1992.                                           eering, Colorado State University, Fort Collins, CO, May,
            Adamson, A. W., Physical Chemistry of Surfaces, 2nd edn., Inter-  1993.
                science Publishers, New York, 1967.            Carter, M. C. and Weber, W. J. Jr., Modeling adsorption of TCE by
            Adamson, A. W. and Gast, A. P., Physical Chemistry of Surfaces,  activated carbon preloaded by background organic matter,
                6th edn., Interscience Publishers, New York, 1997.  Environmental Science and Technology, 28(4):616–623, 1994.
            Alberty, R. A. and Silbey, R. J., Physical Chemistry, 1st edn., John  Charlie, W. A., Personal communication, May 5, 2003.
                Wiley & Sons, New York, 1992.                  Cheremisinoff, P. N. and Ellerbusch, F., Carbon Adsorption Hand-
            AWTR: Advanced Waste Treatment Research Program, Robert A.  book, Ann Arbor Science Publishers, Inc., Ann Arbor, MI,
                Taft Sanitary Engineering Center, Division of Water Supply  1978.
                and Pollution Control, U.S. Public Health Service, Cincinnati,  Clark, R. M. and Lykins, B. W., Granular Activated Carbon—
                OH. As related to activated carbon adsorption, the research in  Design, Operation and Cost, Lewis Publishers, Chelsea, MI,
                this program produced the reports listed below during the  1989.
                period 1961–1968.                              Colorado Springs, City of, Tertiary-Treatment Plant (handout paper
            . Anon., Summary Report: June 1960–December 1961, Advanced  for plant visitors), Colorado Springs, CO, c. 1974.
              Waste Treatment Research-1, May, 1962.           Cookson, J. T., Adsorption mechanisms: The chemistry of organic
            . Anon., Summary Report: Jan 1962–June 1964, Advanced Waste  adsorption on activated carbon, Chap. 7, in: Cheremisinoff,
              Treatment Research, AWTR-14, April, 1965.             P. N. and Ellerbusch, F. (Eds.), Carbon Adsorption Hand-
            . Anon., Summary Report: July 1964–July 1967, Advanced Waste  book, Ann Arbor Science Publishers, Inc., Ann Arbor, MI,
              Treatment Research, AWTR-19, 1968.                    1978.
            . Johnson, R. L., Lowes, F. J. Jr., Smith, R. M., and Powers, T. J.,
                                                               Cookson, J. T. and North, W. J., Adsorption of viruses on activated
              Evaluation of the Use of Activated Carbons in Treatment of Waste-  carbon, Environmental Science and Technology, 1(1):46–52,
              water, AWTR-11, May, 1964.                            January, 1967.
            . Joyce, R. S. and Sukenik, V. A., Feasibility of Granular Acti-  Crittenden, J. C. and Weber, W. J. Jr., Predictive model for design
              vated-Carbon Adsorption for Wastewater Renovation 2, AWTR-  of fixed-bed adsorbers: Parameter estimation and model
              10, October, 1965.                                    development, Journal of the Environmental Engineering
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