The wastewater treatment program established within a facility is influenced by factors such as the nature and volume of the waste streams, discharge limits, available space and the generated waste. The nature and volume of the waste stream and discharge limits will influence the choice of equipment and treatment chemicals. The overall cost of treatment involves operational costs such as energy, labor, treatment chemicals, maintenance and waste disposal. The Resource Conservation and Recovery Act (RCRA) prohibits disposal of sludge/solid waste that does not pass Toxicity Characteristics Leaching Procedure (TCLP). This type of waste is hauled away and treated at waste treatment facilities prior to being landfilled.
Industries that discharge metal-bearing effluent most likely will not be able to meet the proposed limits using conventional hydroxide precipitation alone, which is considered the best available technology (BAT). The industries will have to introduce ion exchange, reverse osmosis or implement a secondary step using a polishing agent such as dithiocarbamate (DTC), in order to achieve the proposed limits. Recently, it has been reported that metal-DTC waste (cadmium, copper, lead and mercury) is unstable, and under the conditions of TCLP testing, the leachate showed levels exceeding RCRA limits. DTC is toxic, and it has deleterious effects on the environment, e.g., the case of the dithiocarbamates spills into the White River in Anderson, Indiana in 1999 that killed more than 80,000 fish along a 50 mile stretch. Aquasil® is a single-step treatment with enhanced efficiency in removing contaminants such as heavy metals, oil and grease, organic matters and suspended solids simultaneously. It employs proprietary advanced materials that are made to fit the chemistry of the particular waste stream. The products are used in both batch and continuous processes, and effluent can be treated at low, neutral or moderately high pH. It overcomes problems associated with hardness and, in most cases, the presence of complexing or chelating agents, surfactants and detergents. Figure 1 illustrates a continuous setup of the treatment. Case Studies The acidic waste stream was treated with the new treatment without any pH adjustment. Analytical data shown in Table 1 indicate that the treatment brought the levels of copper and lead below the new MP&M limits. The treatment produced large, dense floc that settled efficiently. Moreover, the treatment eliminated DTC, caustic and polymer. The treated water can be reused. The treatment also generates less waste, which passes the TCLP test. Case 2: Metal Finishing The pH is adjusted to 9.9-10.4, and a coagulant is added. The wastewater then flows to a flash-mixing tank where a flocculent is added and then to a clarifier. Sludge from the clarifier is pumped to a sludge holding tank and dewatered in a filter press. Treated water flows to the final tank where pH is adjusted to between 6.5-9.5 prior to discharge. The treatability study was done on the wastewater composite (pH = 2-3) without Mg(OH)2 neutralization. The wastewater was treated directly. Large, dense floc formed within a few minutes and settled quite efficiently. The treated effluent was clear and free of pin floc. Filtration was easy and filter cake dried well. Final pH was about 9.5-10. Treatment eliminated the use of magnesium hydroxide, caustic, coagulant and flocculent. Metal concentrations in the effluent are far below the proposed MP&M limits. Table 2 shows analytical results of raw and treated effluent. Moreover, the treatment generated a much drier cake.
Case 3: Aircraft Maintenance Facility A treatability study was conducted on a sample of the oily waste. As a result, one treatment was chosen as the most cost effective technology, and a fully automated batch system was installed to treat the oily waste. Table 3 shows that the system delivered results far below discharge requirements for all parameters. The system achieved almost 100% percent removal of heavy metals and oil and grease and more than 99% of suspended solids. The system requires very little maintenance and only minimal operator attention. Before and after treatment analytical data for the above cases were provided by the respective facilities. All conventional techniques used in the treatment of waste streams produce sludge/waste that can be hazardous due high concentrations of contaminants. Safe disposal of such waste is troublesome and the problem is aggravated by the continued increase in the number of wastewater treatment plants. Currently, waste is transported to treatment plants where it undergoes further treatment to render it suitable for disposal. This adds to the overall cost of treatment. Waste generated by this particular treatment is already stabilized and does not require any further treatment to render it suitable for disposal in a landfill. Characteristic waste passes the TCLP test and meets regulatory requirements for disposal as nonhazardous material. Listed waste also passes the TCLP test and can be disposed of likewise once exclusion has been granted. Table 4 shows TCLP test results for the aircraft maintenance waste (see case 3). This technology is a fast process with enhanced efficiency in removing contaminants such as heavy metals, oil and grease, organic matters and TSS, simultaneously. The treatment lowers the levels of chromium (VI), arsenic, selenium, phosphate, fluoride, TDS, COD and phenol. The treatment is easy to implement and operate, effective, requires less energy and maintenance, delivers high-quality effluent, achieves zero-discharge through the recycle/reuse, and generates nonhazardous waste that does not need further treatment prior to disposal. Moreover, it brings about compliance.
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