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Adsorption                                                                                       493



            William T. Love, an entrepreneur who, in 1892, saw a canal as  1000
            a means for ships to bypass Niagara Falls or, alternatively, to
            generate electric energy. Because of loss of financial backing,
            only 1 mi of the canal was dug, leaving a body of water 60 ft
            wide and 3000 ft long. By 1920, the land was sold and
            afterward became a municipal and chemical disposal site.    200
            From 1942 through 1953, the Love Canal Landfill was used
            principally by Hooker Chemical, one of the many chemical
            plants located along the Niagara River. During this period,  X* (mg SOC/g GAC)  100
            nearly 19,000 metric tons (21,000 U.S. tons) of ‘‘toxic chem-
            icals’’ were dumped at the site. In 1953, with the landfill at
            maximum capacity, Hooker filled the site with layers of soil.
                                                                                                      4200
            Human exposures: The Niagara Falls Board of Education then
            purchased the Love Canal land from Hooker Chemical for $1.
            Included in the deed transfer was a ‘‘warning’’ of the chemical
            wastes buried on the property and a disclaimer absolving  10
            Hooker of any further liability. Single-family housing soon  100             1000                10 4
            surrounded the Love Canal site, and, as the population grew,             C* (mg SOC/L)
            the 99th Street School was built directly on the former landfill.  FIGURE 15.21 Isotherm for aggregate of synthetic organic
            At the time, homeowners were not warned or provided infor-  compounds (SOC) at Love Canal. (Adapted from McDougall, W.J.
            mation of potential hazards associated with the former landfill  et al., J. Water Pollut. Control Federation, 52(12), 2916, December
            site. According to residents who lived in the area, from the  1980.)
            late 1950s through the early 1970s repeated complaints of
            odors and ‘‘substances’’ surfacing in their yards brought City
            officials to visit the neighborhood. By 1978, the Love Canal  A temporary treatment system was set up and included caustic
            neighborhood included approximately 800 private, single-  soda addition, clarification=sludge disposal, filtration, GAC
            family homes, 240 low-income apartments, and the 99th  adsorption, and discharge to sanitary sewer. The GAC treat-
            Street Elementary School—located near the center of the  ment included two skid-mounted pressure reactors, each hold-
            landfill. On August 7, 1978, President Jimmy Carter declared  ing 9,072 kg (20,000 lb) of GAC with Q   662 L=min
            the Love Canal area a federal emergency, which provided  (175 gpm). For this temporary full-scale system, TOC(influ-
            funds to relocate the 239 families living in the first two rows  ent)   800 mg=L and TOC(effluent)   80 mg=L. The Love
            of homes encircling the landfill. By 1980, U.S. government  Canal site was 6.47 ha in area and was essentially a ‘‘bathtub’’
            scientists had identified 248 individual chemicals in the Love  in that it was underlain by bedrock and there was no flow of
            Canal waste site. (The foregoing paragraphs were abstracted  groundwater through the site. Thus, it was a classic ‘‘pump
            from http:==ublib.buffalo.edu=libraries= projects=lovecanal=.)  and treat’’ situation (foregoing from McDougall et al., 1980).
            Chemical conditions: An analysis of composite samples from  GAC performance and observations: Table 15.10 lists the
            14 shallow wells before treatment was started which gave the  priority pollutant compounds (all 29 were found) with con-
            following general results: pH   5.6; TOC   4,300 mg=L;  centrations indicated before and after GAC treatment. Import-
                                                               ant points to note include (1) the data pertain to a mixture;
            SOC   4,200 mg=L; COD   11,500 mg=L; oil=grease
            90 mg=L; suspended solids   200 mg=L; dissolved solids  (2) an isotherm, Figure 15.21, was defined from the SOC
              15,700  mg=L;   chloride   9,500  mg=L;  sulfate    mixture; (3) influent concentrations were high for most com-
            240 mg=L; sodium   1,000 mg=L; calcium   2,500 mg=L;  pounds; (4) GAC treatment reduced most effluent concentra-
            iron   330 mg=L; mercury < 0.0005 mg=L; lead   0.4 mg=L.  tions to ‘‘not detectable’’ (ND); and (5) a ‘‘chromatography
            An equilibrium study of X*(SOC) versus C*(SOC) generated  effect’’ (one or more compounds being displaced by others)
            a well-defined isotherm, Figure 15.21, which showed, for  was not seen.
            example, that at C*(SOC)   4200 mg=L, X*(SOC)   200 mg
            SOC=g GAC.                                         15.4.3.4.2  Rocky Mountain Arsenal, Colorado
                                                               The Rocky Mountain Arsenal in Colorado, near Denver, was
            GAC pilot plant: A GAC pilot system was used to assess
                                                               a9.66km   8.66 km (6 mi   6 mi) area of land located on the
            treatment parameters, consisting of two columns in series,
                                                               NE side of Denver and about 5 km east of the South Platte
            each 1.2 m (4 ft) long. The first-stage column was removed
                                                               River, which flows in a northerly direction. Groundwater flow
            from operation when the breakthrough occurred in the effluent
                                                               through a shallow aquifer is north-west, toward the South
            from the second-stage column (simulating full-scale oper-
                                                               Platte.
            ation). The effluent TOC was about 260 mg=L. Figure 15.21
            shows an isotherm generated for the aggregate SOCs at the  Background: The site was developed during WWII to manu-
            site. The pilot study also indicated the rate of carbon exhaus-  facture munitions; nerve gas was the most prominent. The
                               3
            tion as 34 kg GAC=m water treated (284 lb=1000 gal).  facility was taken over, by lease arrangement beginning in
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